WO2025205198A1 - Substance transfer device and transfer method, and method for removing internal residue in apparatus for substance - Google Patents
Substance transfer device and transfer method, and method for removing internal residue in apparatus for substanceInfo
- Publication number
- WO2025205198A1 WO2025205198A1 PCT/JP2025/010311 JP2025010311W WO2025205198A1 WO 2025205198 A1 WO2025205198 A1 WO 2025205198A1 JP 2025010311 W JP2025010311 W JP 2025010311W WO 2025205198 A1 WO2025205198 A1 WO 2025205198A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- substance
- transfer
- inert gas
- container
- inlet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G65/00—Loading or unloading
- B65G65/30—Methods or devices for filling or emptying bunkers, hoppers, tanks, or like containers, of interest apart from their use in particular chemical or physical processes or their application in particular machines, e.g. not covered by a single other subclass
- B65G65/34—Emptying devices
- B65G65/40—Devices for emptying otherwise than from the top
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0561—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of inorganic materials only
- H01M10/0562—Solid materials
Definitions
- Known methods for producing solid electrolytes used in solid electrolyte layers include, for example, a method for producing a solid electrolyte that involves mixing a complexing agent and a solid electrolyte raw material to prepare an electrolyte precursor (see, for example, Patent Document 1), and a method for producing a solid electrolyte that involves drying a slurry containing a complexing agent and an electrolyte precursor by fluidized drying using media particles (see, for example, Patent Document 2).
- the present invention was made in light of these circumstances, and aims to provide a substance transfer device and method, as well as a method for removing internal residues from substance-handling equipment, that can safely and efficiently handle substances containing at least one atom selected from sulfur atoms and halogen atoms.
- the substance transfer device comprises: An apparatus for transferring a substance containing at least one atom selected from a sulfur atom and a halogen atom,
- the apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism, the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container; the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber; material transfer equipment, is.
- the method for transferring a substance comprises:
- the apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism, the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
- the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber; using a transfer device for a substance containing at least one atom selected from a sulfur atom and a halogen atom,
- a method for transferring a substance, comprising the steps of (1A) to (3A) below: is.
- the method for removing internal residues from a substance container comprises:
- the apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism, the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
- the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber; using a transfer device for a substance containing at least one atom selected from a sulfur atom and a halogen atom,
- a method for removing internal residues from a substance container comprising the steps of (1B) and (2B) below: is.
- the transfer substance inlet is connected to the valve 1a provided at the substance outlet of the first substance container.
- the valve 1a is opened, and the inert gas is supplied and discharged by the inert gas introduction mechanism and discharge mechanism, filling the inert gas into the preliminary substance chamber and the first substance container.
- the present invention provides a substance transfer device and method, as well as a method for removing internal residues from substance-handling equipment, that can safely and efficiently handle substances containing at least one atom selected from sulfur atoms and halogen atoms.
- FIG. 1 is a schematic diagram showing a preferred embodiment of a substance transfer device according to the present embodiment.
- 1 is a schematic diagram showing a preferred embodiment of a substance transfer device according to the present embodiment.
- this embodiment An embodiment of the present invention (hereinafter sometimes referred to as “this embodiment") will be described below.
- the upper and lower limit values of numerical ranges expressed as "greater than or equal to,” “less than or equal to,” and “to” can be arbitrarily combined, and numerical values in examples can also be used as upper and lower limit values.
- preferred specifications can be adopted arbitrarily. In other words, one preferred specification can be adopted in combination with one or more other preferred specifications. It can be said that combinations of preferred items are more preferable.
- Hydrogen sulfide can be generated when a substance containing sulfur atoms comes into contact with moisture in the air, for example, when the substance is transferred between one container and another, so caution is required. Furthermore, just like substances containing sulfur atoms, caution is also required regarding safety when transferring substances containing halogen atoms.
- the dispersion device described in Patent Document 3 above is designed to supply dry gas while supplying powder to prevent the powder from reacting with moisture, which can cause deterioration and decomposition of the powder, resulting in performance degradation and the generation of toxic gas (Patent Document 3, paragraph [0008]).
- the dispersion device described in Patent Document 3 is designed for normal operation, in which powder is supplied to the stirring and mixing section together with dry gas and mixed with liquid, and the only locations that are subject to a dry gas atmosphere are those through which powder passes during normal operation, i.e., the powder supply section and the stirring and mixing section. Therefore, no consideration is given to locations where substances such as powder do not flow during normal operation.
- the mixing system described in Patent Document 4 has a hopper equipped with a dry gas supply unit and a mixing mechanism connected in a state isolated from the outside air, thereby attempting to mix materials such as liquids and powders without contacting moisture in the outside air and exposing these materials to a dry gas environment (paragraphs [0038], [0044], etc.).
- the mixing system described in Patent Document 4 also assumes normal operation, in which multiple materials and dry gas coexist and are mixed inside the device, and the only areas that are subject to a dry gas environment are the hopper and mixing mechanism, which are areas through which powder passes during normal operation. Therefore, like Patent Document 3, Patent Document 4 also makes no consideration whatsoever to areas where powder and other substances do not flow during normal operation.
- the inventors investigated methods for handling the above-mentioned substances, which arise in all situations, such as during the start-up, normal operation, shutdown, and maintenance of manufacturing equipment, and methods for ensuring safety, particularly during transfer, by minimizing reactions between the substances and moisture in the atmosphere.
- a spare chamber capable of storing an inert gas, such as nitrogen, as a transfer device.
- an inert gas such as nitrogen
- Patent documents 3 and 4 do not mention at all the following: the preliminary chamber, through which the substance flows when transferring from one container to another, is filled with an inert gas atmosphere; however, the preliminary chamber, through which the substance does not flow during normal operation; or the use of the system in situations other than normal operation, such as connecting one container to another when transferring a substance stored in one container to that other container.
- the interior may be cleaned in advance with a fluid such as water.
- a fluid such as water.
- This may cause a reaction between the water used for cleaning and the above-mentioned substances, in addition to the moisture in the atmosphere.
- the water used for cleaning may then remain inside the equipment. Therefore, in order to perform maintenance more safely and quickly after shutting down the manufacturing facility, it is also important to more efficiently remove the water used for cleaning that remains inside the equipment.
- the transfer device and method of the present invention for a substance containing at least one atom selected from sulfur atoms and halogen atoms, as well as the method for removing internal residues from a substance-transporting device, can handle the above-mentioned substance safely and efficiently.
- the substance transfer device includes: An apparatus for transferring a substance containing at least one atom selected from a sulfur atom and a halogen atom,
- the apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism, the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
- the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber; material transfer equipment, is.
- the material transfer device when transferring a material containing sulfur atoms, such as lithium sulfide, diphosphorus pentasulfide, or elemental sulfur, or a material containing halogen atoms, such as lithium halide or elemental halogen, from a first container to a second container (or from the second container to the first container), safety can be ensured by suppressing reactions between the material and moisture in the atmosphere, etc., with a simple structure that includes a transfer reserve chamber, a transfer material inlet and outlet, and an inert gas introduction and exhaust mechanism. Furthermore, because safety can be ensured, work efficiency can be improved. As a result, it becomes possible to safely and efficiently handle a material containing at least one atom selected from sulfur atoms and halogen atoms (hereinafter sometimes simply referred to as "material").
- material containing at least one atom selected from sulfur atoms and halogen atoms
- a substance transfer device includes: The substance transfer apparatus according to the first aspect, wherein the inert gas introduction mechanism further introduces the inert gas from an inert gas inlet provided in the first substance container. is.
- the inert gas introduction mechanism can introduce inert gas through an inert gas inlet provided in the first substance container, allowing for safer and more efficient handling of substances. Furthermore, when removing internal residue from the substance container (described below), this can be done more efficiently, which can also improve the operating rate of the manufacturing equipment.
- a substance transfer device includes: The substance transfer apparatus according to the first or second aspect, wherein the transfer preliminary chamber is cylindrical. is.
- the transfer pre-chamber is cylindrical, it is possible to ensure safety while, in particular, transferring materials more smoothly, making it possible to handle materials more safely and efficiently. It also improves the maintainability of the material transfer device.
- a substance transfer device includes: The substance transfer device according to the third aspect, wherein the transfer substance inlet portion and the transfer substance outlet portion are provided at both ends of the cylindrical transfer pre-chamber. is.
- a substance transfer device includes: The substance transfer apparatus according to the third or fourth aspect, wherein the inert gas introduction mechanism and discharge mechanism are provided on a side surface of the cylindrical transfer pre-chamber. is.
- This type of structure allows for more stable introduction and discharge of inert gas, ensuring safety and particularly facilitating smoother transfer of materials, making it possible to handle materials more safely and efficiently.
- a method for transferring a substance includes:
- the apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism, the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
- the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber; using a transfer device for a substance containing at least one atom selected from a sulfur atom and a halogen atom,
- a method for transferring a substance, comprising the steps of (1A) to (3A) below: is.
- the transfer substance inlet portion is connected to a valve 1a provided at the substance outlet portion of the first substance container, and the transfer substance outlet portion is connected to a valve 2 provided at the second substance transfer port portion of the second substance container.
- the valves 1a and 2 are closed, and the inert gas is supplied and discharged by the inert gas introduction mechanism and discharge mechanism, filling the inert gas into the transfer preliminary chamber.
- (3A) The supply and discharge of the inert gas are stopped, the valves 1a and 2 are opened, and the substance stored in the first substance container is transferred to the second substance container.
- a substance transfer method includes: The method for transferring a substance according to the sixth aspect, comprising carrying out the operations (2A) and (4A) and (5A) below after the operation (3A); is. (4A) The second substance container and valve 2 are removed from the transfer substance outlet. (5A) A closing flange is attached to the outlet portion of the transfer substance.
- a method for removing internal residue from a substance container includes:
- the apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism, the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
- the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber; using a transfer device for a substance containing at least one atom selected from a sulfur atom and a halogen atom,
- a method for removing internal residues from a substance container, comprising the steps of (1B) and (2B) below: is.
- the transfer substance inlet is connected to the valve 1a provided at the substance outlet of the first substance container.
- the valve 1a is opened, and the inert gas is supplied and discharged by the inert gas introduction mechanism and discharge mechanism, filling the inert gas into the transfer pre-chamber and the first substance container.
- the inside of the equipment may be washed with a fluid such as water beforehand, and this may cause a reaction between not only the moisture in the air but also the water used for washing and the above-mentioned substances.
- the medium such as water used for washing, as well as the substances themselves, may remain inside the equipment.
- the method for removing internal residue from a substance container of this embodiment employs the substance transfer apparatus of this embodiment.
- a method for removing internal residue from a substance container includes: the inert gas introduction mechanism introduces an inert gas from an inert gas inlet provided in the first container for the substance; is.
- introducing inert gas from the first substance container also makes it possible to more efficiently remove internal residue from the substance container. As a result, substances can be handled more safely and efficiently, and the operating rate of the manufacturing equipment can also be improved.
- the substance transfer device of this embodiment is An apparatus for transferring a substance containing at least one atom selected from a sulfur atom and a halogen atom,
- the apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism, the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container; the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber; This is the device.
- the substance to be transferred in the substance transfer device of this embodiment is not particularly limited as long as it contains at least one atom selected from sulfur atoms and halogen atoms.
- examples of the substance containing sulfur atoms include a solid electrolyte raw material containing sulfur atoms; an electrolyte precursor when a complexing agent is used, an intermediate such as a heat-treated product obtained by heat treatment in a solvent using a pressure-resistant container when a pressure-resistant container is used; and a sulfide solid electrolyte that will be the product.
- substances containing halogen atoms include solid electrolyte raw materials containing halogen atoms; electrolyte precursors when a complexing agent is used, intermediates such as heat-treated products obtained by heat treatment using a pressure-resistant vessel when a pressure-resistant vessel is used; and sulfide solid electrolyte products that will be the product.
- substances containing sulfur atoms and halogen atoms include intermediates such as electrolyte precursors and heat-treated products obtained using the above-mentioned solid electrolyte raw materials containing sulfur atoms and solid electrolyte raw materials containing halogen atoms; and sulfide solid electrolyte products that will be the product. Details of these solid electrolyte raw materials, intermediates, and sulfide solid electrolytes will be provided below.
- substances containing at least one atom selected from sulfur atoms and halogen atoms are solid electrolyte raw materials, intermediates, and sulfide solid electrolytes, and are basically in the form of powder, but may also be in the form of a liquid or a slurry containing powder.
- the equipment constituting the sulfide solid electrolyte production apparatus to which it is connected may vary depending on the sulfide solid electrolyte production method, but mainly includes reaction equipment used for reacting the solid electrolyte raw materials; when a solvent (including a complexing agent) is used, heating equipment for removing the solvent (including a complexing agent) from a slurry or solution containing the solid electrolyte raw materials and/or intermediates such as an electrolyte precursor and the solvent (including a complexing agent); heating equipment for crystallization, etc.; separation equipment for separating the sulfide solid electrolyte; particle size adjustment equipment for adjusting the particle size of the sulfide solid electrolyte; when heat treatment is performed using a pressure-resistant container, heating equipment for firing the pressure-resistant container and the heat-treated product; piping connecting these devices; and material containers for storing the above-mentioned materials.
- the transfer substance inlet and outlet ports of the substance transfer device are provided in the transfer preparation chamber, and are preferably provided at both ends of the transfer preparation chamber as shown in Figure 1. Furthermore, the transfer substance inlet and outlet ports of the substance transfer device can be connected to the first substance inlet and first substance outlet ports of the first substance container and the second substance transfer port of the second substance container; in Figure 1 they are connected to the first substance outlet port of the first substance container and the second substance transfer port of the second substance container, respectively, and the substance transfer device of this embodiment is shown as being configured to connect the first substance container and the second substance container.
- FIG. 1 shows that the inert gas introduction mechanism and exhaust mechanism are provided in the transfer pre-chamber, and can introduce and exhaust the inert gas into the transfer pre-chamber.
- FIG. 1 also shows that, in a preferred embodiment, the inert gas introduction mechanism further introduces the inert gas from an inert gas inlet provided in the first substance container.
- the length of the piping portion should usually be between 10 cm and 1 m.
- the transfer substance inlet and outlet provided in the preliminary transfer chamber are not particularly limited as long as they can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container, and for example, when the preliminary transfer chamber is cylindrical (configured by piping), it is preferable that they be provided at both ends of the cylinder (piping) as shown in Figure 1. This makes it easier to connect the first substance container and the second substance container, improving the convenience of the substance transfer device of this embodiment.
- the inert gas introduction mechanism is not particularly limited as long as it can introduce the inert gas into the transfer preparatory chamber, and preferably includes, for example, a connection part for receiving the inert gas from an inert gas supply source, a pipe from the connection part to the transfer preparatory chamber, and a gate valve in the pipe, as shown in Fig. 1.
- a connection part for receiving the inert gas from an inert gas supply source a pipe from the connection part to the transfer preparatory chamber, and a gate valve in the pipe, as shown in Fig. 1.
- the transfer method described below can be performed more easily, improving convenience.
- the inert gas introduction mechanism is preferably provided on the side surface thereof. More specifically, the piping for supplying the inert gas from the connecting portion to the preliminary transfer chamber is preferably connected to the side surface of the preliminary transfer chamber. This connection allows for more stable introduction of the inert gas, thereby ensuring safety and enabling smoother transfer of substances, among other things, and enabling safer and more efficient handling of substances.
- the piping for supplying the inert gas from the connecting part to the transfer preparation chamber may be connected to the transfer preparation chamber by a connection method such as a pipe joint with a flange or a screw, or may be directly connected to the transfer preparation chamber as shown in FIG. 1.
- the inert gas exhaust mechanism is not particularly limited as long as it can exhaust the inert gas from the transfer preparatory chamber.
- it is preferable that it includes a connection section that exhausts the inert gas from the transfer preparatory chamber to an inert gas exhaust line, piping to the connection section, and a gate valve within the piping.
- a gate valve makes it easier to carry out the transfer method described below, improving convenience.
- the substance transfer method of this embodiment includes: The apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism, the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container; the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber; using a transfer device for a substance containing at least one atom selected from a sulfur atom and a halogen atom,
- a method for transferring a substance, comprising the steps of (1A) to (3A) below: is.
- the material transfer method of this embodiment employs the material transfer device of this embodiment.
- the configuration of the material transfer device employed in the material transfer method of this embodiment is as described above for the material transfer device of this embodiment.
- the second substance container which transfers and stores the substance, can be safely removed from the first substance container.
- operation (4A) below can be performed safely, and the removed second substance container can be transported to the desired location.
- operation (5A) it is possible to isolate the first substance container from the outside air. Even if substance remains inside the first substance container and passes through valve 1a, it will be stored in the substance transfer device filled with inert gas, and the closing flange prevents atmospheric air containing moisture from entering the substance transfer device. This prevents the substance from reacting with moisture in the atmosphere, allowing for safe handling of the substance.
- the substance transfer method of this embodiment is intended to be a method of transferring a substance from a first substance container to a second substance container.
- the first substance container and the second substance container are containers used for various purposes, such as mixing, drying, grinding, storing, preserving, and transferring substances.
- the first substance container is used for purposes such as mixing, drying, grinding, and storing substances
- the second substance container is a container used to transfer the substance stored in the first substance container to another location.
- a sulfide solid electrolyte produced by a sulfide solid electrolyte production apparatus and stored in the first substance container is shipped as a product in the second substance container into which the sulfide solid electrolyte was transferred.
- Figure 1 describes a "first substance inlet (outlet)" and a “first substance outlet (inlet),” and the first substance inlet can be a first substance outlet, and the first substance outlet can be a first substance inlet.
- Figure 2 by connecting the first substance container and the second substance container via the substance transfer device of this embodiment, it is possible to transfer the substance stored in the second substance container to the first substance container.
- a method for transferring a substance according to another embodiment different from the method for transferring a substance according to this embodiment includes the following steps:
- the apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism, the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
- the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber; using a transfer device for a substance containing at least one atom selected from a sulfur atom and a halogen atom,
- a method for transferring a substance comprising the following operations (1B) to (3B): (1B)
- the transfer substance inlet portion is connected to a valve 2 provided at the second substance transfer port portion of the second substance container, and the transfer substance outlet portion is connected
- the first substance container is used for purposes such as mixing, drying, grinding, and storing substances
- the second substance container is a container used to transfer an object received at a location separate from the first substance container to the first substance container. More specifically, for example, a solid electrolyte raw material that is commercially available or produced by a different manufacturing device is transferred to the second substance container, the second substance container storing the solid electrolyte raw material is connected to the first substance container via a substance transfer device, and the solid electrolyte raw material is transferred from the second substance container to the first substance container and used to produce a sulfide solid electrolyte.
- the substance can be transferred to the second substance container in a manner similar to the substance transfer method of this embodiment.
- the method for removing internal residues from a substance container includes the steps of:
- the apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism, the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
- the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber; using a transfer device for a substance containing at least one atom selected from a sulfur atom and a halogen atom,
- a method for removing internal residues from a substance container comprising the steps of (1B) and (2B) below: is.
- the transfer substance inlet is connected to the valve 1a provided at the substance outlet of the first substance container.
- the valve 1a is opened, and the inert gas is supplied and discharged by the inert gas introduction mechanism and discharge mechanism, filling the inert gas into the transfer pre-chamber and the first substance container.
- the substance transfer device of this embodiment is used to perform the operations (1B) and (2B) described above.
- Valve 1a used in operations (1B) and (2B) is shown in Figure 1 as being provided in the first substance container and the second substance container, but it may also be a valve provided in the substance transfer device.
- an inert gas through an inert gas inlet provided in the first substance container using an inert gas introduction mechanism. This makes it possible to more efficiently remove internal residues from the substance container. As a result, substances can be handled more safely and efficiently, and the operating rate of the manufacturing equipment can also be improved.
- the substance transfer device, substance transfer method, and method for removing internal residue from a substance container of this embodiment are suitable for use in a sulfide solid electrolyte manufacturing device.
- the sulfide solid electrolyte obtained by the sulfide solid electrolyte manufacturing device has high ionic conductivity, and is therefore suitable for use as a solid electrolyte or electrode composite in lithium ion batteries, particularly lithium ion batteries used in information-related devices and communication devices such as personal computers, video cameras, and mobile phones, as well as vehicles such as automobiles, and particularly all-solid-state batteries.
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Abstract
Description
本発明は、物質の移送装置及び移送方法並びに物質用機器の内部残留物の除去方法に関する。 The present invention relates to a substance transfer device and transfer method, as well as a method for removing internal residue from substance-transfer equipment.
近年におけるパソコン、ビデオカメラ、及び携帯電話等の情報関連機器や通信機器等の急速な普及に伴い、その電源として利用される電池の開発が重要視されている。従来、このような用途に用いられる電池において可燃性の有機溶媒を含む電解液が用いられていたが、電解液が液体であり、かつ可燃性であることから、電池として用いた場合に、漏洩、発火等に関する安全性が懸念されている。特に、車載用途においては、高容量化、高出力化が求められており、従来の電解液を用いた電池における安全性への懸念は大きくなる一方である。そこで、電池を全固体化することで、電池内に可燃性の有機溶媒を用いず、安全装置の簡素化が図れ、製造コスト、生産性に優れることから、電解液を固体電解質層に換えた全固体電池の開発が行われている。 With the rapid spread of information-related and communication devices such as personal computers, video cameras, and mobile phones in recent years, the development of batteries to be used as their power sources has become increasingly important. Traditionally, batteries used in these applications have used electrolytes containing flammable organic solvents. However, because the electrolyte is liquid and flammable, safety concerns regarding leakage and fire have arisen when used in batteries. In particular, demand for higher capacity and output is growing for automotive applications, and safety concerns regarding batteries that use conventional electrolytes are growing. Therefore, all-solid-state batteries, which replace the electrolyte with a solid electrolyte layer, are being developed, as this eliminates the use of flammable organic solvents in the battery, simplifies safety devices, and offers superior manufacturing costs and productivity.
固体電解質層に用いられる固体電解質の製造方法としては、例えば、錯化剤と固体電解質原料とを混合して電解質前駆体を調製することを含む固体電解質の製造方法(例えば、特許文献1参照)、また錯化剤及び電解質前駆体を含むスラリーを、メディア粒子を用いた流動乾燥により乾燥することを含む固体電解質の製造方法(例えば、特許文献2参照)等が知られている。 Known methods for producing solid electrolytes used in solid electrolyte layers include, for example, a method for producing a solid electrolyte that involves mixing a complexing agent and a solid electrolyte raw material to prepare an electrolyte precursor (see, for example, Patent Document 1), and a method for producing a solid electrolyte that involves drying a slurry containing a complexing agent and an electrolyte precursor by fluidized drying using media particles (see, for example, Patent Document 2).
粉体を扱う系において、粉体と液体を混合する撹拌混合部と、撹拌混合部に粉体を供給する、密封可能な粉体供給部と、粉体供給部にドライガスを供給するドライガス発生部と、を備える分散装置が開示されている(例えば、特許文献3)。また、複数の材料を混合する混合システムにおいて、複数の材料を混合する混合機構、及び材料を調整する材料調整部と、材料を混合機構に供給する注ぎ口部とを具備するホッパー内にドライガスを供給するドライガス供給部を有することが記載されている(例えば、特許文献4) In a powder handling system, a dispersion device has been disclosed that includes a stirring/mixing section that mixes powder and liquid, a sealable powder supply section that supplies powder to the stirring/mixing section, and a dry gas generator that supplies dry gas to the powder supply section (see, for example, Patent Document 3). Also, in a mixing system that mixes multiple materials, a dry gas supply section that supplies dry gas to a hopper equipped with a mixing mechanism that mixes multiple materials, a material adjustment section that adjusts the materials, and a spout that supplies the materials to the mixing mechanism (see, for example, Patent Document 4).
本発明は、このような状況に鑑みてなされたものであり、安全かつ効率的に、硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質を取扱いし得る、物質の移送装置及び移送方法並びに物質用機器の内部残留物の除去方法を提供することである。 The present invention was made in light of these circumstances, and aims to provide a substance transfer device and method, as well as a method for removing internal residues from substance-handling equipment, that can safely and efficiently handle substances containing at least one atom selected from sulfur atoms and halogen atoms.
本発明に係る物質の移送装置は、
硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質の移送装置であり、
移送用予備室と、移送物質入口部及び移送物質出口部と、不活性ガスの導入機構及び排出機構と、を備え、
前記移送物質入口部及び移送物質出口部は、前記移送用予備室に設けられ、かつ物質用第一容器の第一物質入口部及び第一物質出口部並びに物質用第二容器の第二物質移送口部と連結可能であり、
前記不活性ガスの導入機構は前記移送用予備室に不活性ガスを導入し、前記不活性ガスの排出機構は前記移送用予備室から不活性ガスを排出する、
物質移送装置、
である。
The substance transfer device according to the present invention comprises:
An apparatus for transferring a substance containing at least one atom selected from a sulfur atom and a halogen atom,
The apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism,
the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber;
material transfer equipment,
is.
本発明に係る物質の移送方法は、
移送用予備室と、移送物質入口部及び移送物質出口部と、不活性ガスの導入機構及び排出機構と、を備え、
前記移送物質入口部及び移送物質出口部は、前記移送用予備室に設けられ、かつ物質用第一容器の第一物質入口部及び第一物質出口部並びに物質用第二容器の第二物質移送口部と連結可能であり、
前記不活性ガスの導入機構は前記移送用予備室に不活性ガスを導入し、前記不活性ガスの排出機構は前記移送用予備室から不活性ガスを排出する、
硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質の移送装置を用い、
下記(1A)~(3A)の操作を行う、物質の移送方法、
である。
(1A)前記移送物質入口部と前記物質用第一容器の物質出口部に設けられた弁1aとを連結し、前記移送物質出口部と前記物質用第二容器の第二物質移送口部に設けられた弁2とを連結する。
(2A)前記弁1a及び弁2を閉とし、前記不活性ガスの導入機構及び排出機構により不活性ガスの供給及び排出を行い、不活性ガスを前記移送用予備室に充填する。
(3A)前記不活性ガスの供給及び排出を停止し、前記弁1a及び弁2を開とし、前記物質用第一容器に貯留される物質を、前記物質用第二容器に移送する。
The method for transferring a substance according to the present invention comprises:
The apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism,
the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber;
using a transfer device for a substance containing at least one atom selected from a sulfur atom and a halogen atom,
A method for transferring a substance, comprising the steps of (1A) to (3A) below:
is.
(1A) The transfer substance inlet portion is connected to a valve 1a provided at the substance outlet portion of the first substance container, and the transfer substance outlet portion is connected to a valve 2 provided at the second substance transfer port portion of the second substance container.
(2A) The valves 1a and 2 are closed, and the inert gas is supplied and discharged by the inert gas introduction mechanism and discharge mechanism, filling the inert gas into the transfer preliminary chamber.
(3A) The supply and discharge of the inert gas are stopped, the valves 1a and 2 are opened, and the substance stored in the first substance container is transferred to the second substance container.
本発明に係る物質用容器の内部残留物の除去方法は、
移送用予備室と、移送物質入口部及び移送物質出口部と、不活性ガスの導入機構及び排出機構と、を備え、
前記移送物質入口部及び移送物質出口部は、前記移送用予備室に設けられ、かつ物質用第一容器の第一物質入口部及び第一物質出口部並びに物質用第二容器の第二物質移送口部と連結可能であり、
前記不活性ガスの導入機構は前記移送用予備室に不活性ガスを導入し、前記不活性ガスの排出機構は前記移送用予備室から不活性ガスを排出する、
硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質の移送装置を用い、
下記(1B)及び(2B)の操作を行う、物質用容器の内部残留物の除去方法、
である。
(1B)前記移送物質入口部と前記物質用第一容器の物質出口部に設けられた弁1aとを連結する。
(2B)前記弁1aを開とし、前記不活性ガスの導入機構及び排出機構により不活性ガスの供給及び排出を行い、不活性ガスを前記物質用予備室及び前記物質用第一容器に充填する。
The method for removing internal residues from a substance container according to the present invention comprises:
The apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism,
the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber;
using a transfer device for a substance containing at least one atom selected from a sulfur atom and a halogen atom,
A method for removing internal residues from a substance container, comprising the steps of (1B) and (2B) below:
is.
(1B) The transfer substance inlet is connected to the valve 1a provided at the substance outlet of the first substance container.
(2B) The valve 1a is opened, and the inert gas is supplied and discharged by the inert gas introduction mechanism and discharge mechanism, filling the inert gas into the preliminary substance chamber and the first substance container.
本発明によれば、安全かつ効率的に、硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質を取扱いし得る、物質の移送装置及び移送方法並びに物質用機器の内部残留物の除去方法を提供することができる。 The present invention provides a substance transfer device and method, as well as a method for removing internal residues from substance-handling equipment, that can safely and efficiently handle substances containing at least one atom selected from sulfur atoms and halogen atoms.
以下、本発明の実施形態(以下、「本実施形態」と称することがある。)について説明する。なお、本明細書において、「以上」、「以下」、「~」の数値範囲に係る上限及び下限の数値は任意に組み合わせできる数値であり、また実施例の数値を上限及び下限の数値として用いることもできる。また、好ましいとされている規定は任意に採用することができる。即ち、好ましいとされている一の規定を、好ましいとされている他の一又は複数の規定と組み合わせて採用することができる。好ましいもの同士の組み合わせはより好ましいといえる。 An embodiment of the present invention (hereinafter sometimes referred to as "this embodiment") will be described below. Note that in this specification, the upper and lower limit values of numerical ranges expressed as "greater than or equal to," "less than or equal to," and "to" can be arbitrarily combined, and numerical values in examples can also be used as upper and lower limit values. Furthermore, preferred specifications can be adopted arbitrarily. In other words, one preferred specification can be adopted in combination with one or more other preferred specifications. It can be said that combinations of preferred items are more preferable.
(本発明に至るために本発明者らが得た知見)
本発明者らは、上記の課題を解決するべく鋭意検討した結果、下記の事項を見出し、本発明を完成するに至った。
(Findings Obtained by the Inventors to Achieve the Present Invention)
As a result of extensive research aimed at solving the above problems, the present inventors have discovered the following and have completed the present invention.
全固体電池の実用化の検討が進められている中、硫化物固体電解質の量産化が喫緊の課題となっている。近年、硫化物固体電解質の需要が高まるにつれて、ラボスケールの設備から量産化に向けたプラントスケールの設備による本格操業が開始している。硫化物固体電解質の製造方法としては、例えば上記特許文献1及び2等の製造方法が検討されており、硫化物固体電解質の製造装置においては、例えば硫化リチウム、五硫化二リン、単体硫黄等の硫黄原子を含む固体電解質原料、これらの固体電解質原料と錯化剤とからなる電解質前駆体、また製品となる硫化物固体電解質等の、硫黄原子を含む様々な物質が取り扱われる。これらの硫黄原子を含む物質は、大気中の水分等と反応して硫化水素を発生する場合があるため、常に安全性に留意する必要がある。 As research into the practical application of all-solid-state batteries progresses, mass production of sulfide solid electrolytes has become an urgent issue. In recent years, as demand for sulfide solid electrolytes has increased, full-scale operations have begun, shifting from lab-scale facilities to plant-scale facilities geared toward mass production. Methods for producing sulfide solid electrolytes, such as those described in Patent Documents 1 and 2, are being considered. Sulfide solid electrolyte production equipment handles a variety of substances containing sulfur atoms, including solid electrolyte raw materials containing sulfur atoms, such as lithium sulfide, diphosphorus pentasulfide, and elemental sulfur; electrolyte precursors composed of these solid electrolyte raw materials and complexing agents; and the resulting sulfide solid electrolyte. Since these sulfur-containing substances can react with moisture in the air and generate hydrogen sulfide, safety must always be taken into consideration.
また、硫化物固体電解質の製造にあたり、主に固体電解質のイオン伝導度を向上させるために、ハロゲン原子を含む物質、例えばハロゲン化リチウム、ハロゲン単体等の物質が固体電解質原料として用いられる。ハロゲン原子を含む物質の中でも、ハロゲン単体は水との反応性が高く、安全性に留意する必要がある。 Furthermore, when manufacturing sulfide solid electrolytes, substances containing halogen atoms, such as lithium halides and elemental halogens, are used as solid electrolyte raw materials, primarily to improve the ionic conductivity of the solid electrolyte. Among substances containing halogen atoms, elemental halogens are highly reactive with water, so safety must be taken into consideration.
硫黄原子を含む物質と大気中の水分等との接触による硫化水素の発生は、例えば物質の一の容器と他の容器との間における移送の際に生じ得るため、留意する必要が生じる。また、ハロゲン原子を含む物質も、硫黄原子を含む物質と同様に、移送の際に安全性に留意する必要が生じる。 Hydrogen sulfide can be generated when a substance containing sulfur atoms comes into contact with moisture in the air, for example, when the substance is transferred between one container and another, so caution is required. Furthermore, just like substances containing sulfur atoms, caution is also required regarding safety when transferring substances containing halogen atoms.
例えば、既述のような硫化リチウム、五硫化二リン、単体硫黄等の硫黄原子を含む固体電解質原料、またハロゲン化リチウム、ハロゲン単体等のハロゲン原子を含む固体電解質原料としては、市販品を使用する、又は別の製造装置で製造したものが用いられる。これらの市販品又は製造品が収納される一の容器から、硫化物固体電解質の製造装置が備える固体電解質原料を貯蔵する他の容器に収納する際、一の容器と他の容器との着脱の際に、何らの手立てがなければ、物質を移送させるための移送用配管内の大気、また周辺の大気と接触するため、安全性に留意する必要がある。また、これと同様の場合としては、硫化物固体電解質の製造装置で得られた硫化物固体電解質を、製品として用途先に搬送する場合、硫化物固体電解質を貯留する一の容器から、硫化物固体電解質を搬送するための容器に移送する場合も挙げられる。
このように、硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を有する物質を一の容器から他の容器に移送しようとすると、物質と大気との接触が生じることがある。
For example, solid electrolyte raw materials containing sulfur atoms, such as lithium sulfide, diphosphorus pentasulfide, and elemental sulfur, as well as solid electrolyte raw materials containing halogen atoms, such as lithium halide and elemental halogen, are commercially available or manufactured in a separate manufacturing apparatus. When transferring these commercially available or manufactured products from one container to another container for storing the solid electrolyte raw material provided in the sulfide solid electrolyte manufacturing apparatus, if no measures are taken when attaching or detaching the one container to the other, the material will come into contact with the atmosphere in the transfer piping for transferring the material and the surrounding atmosphere, so safety must be taken into consideration. Similar cases include when the sulfide solid electrolyte obtained in the sulfide solid electrolyte manufacturing apparatus is transported to its intended use as a product, or when it is transferred from one container storing the sulfide solid electrolyte to a container for transporting the sulfide solid electrolyte.
Thus, when a substance having at least one atom selected from sulfur atoms and halogen atoms is to be transferred from one container to another, the substance may come into contact with the atmosphere.
上記特許文献1及び2に記載される硫化物固体電解質の製造方法を行い得る硫化物固体電解質の製造装置等の物質が流通する製造装置では、運転開始、通常運転、運転停止及びメンテナンス作業等のあらゆる場面において、物質の取扱いが発生し、物質と大気中の水分等との反応による硫化水素の発生に留意する必要がある。しかし、物質の取扱いに関し、何らの考慮もされていない。 In manufacturing equipment through which materials flow, such as sulfide solid electrolyte manufacturing equipment capable of carrying out the sulfide solid electrolyte manufacturing methods described in Patent Documents 1 and 2, materials must be handled in all situations, including during start-up, normal operation, shutdown, and maintenance work, and care must be taken to prevent the generation of hydrogen sulfide due to reactions between the materials and moisture in the air, etc. However, no consideration is given to the handling of materials.
上記特許文献3に記載される分散装置は、粉体と水分が反応することで粉体の変質及び分解が生じ、性能の劣化、有毒ガスの発生が懸念されるところ、粉体と大気中の水分との反応を抑制するため、ドライガスを供給しながら粉体を供給する、というものである(特許文献3、段落〔0008〕)。しかし、特許文献3に記載の分散装置は、粉体をドライガスとともに撹拌混合部に供給して液体と混合させるという通常運転時を前提としており、ドライガス雰囲気とする対象箇所は、粉体が通常運転で通過する箇所、すなわち粉体供給部及び撹拌混合部だけである。そのため、粉体等の物質が通常運転で流通しない箇所については、一切考慮されていない。 The dispersion device described in Patent Document 3 above is designed to supply dry gas while supplying powder to prevent the powder from reacting with moisture, which can cause deterioration and decomposition of the powder, resulting in performance degradation and the generation of toxic gas (Patent Document 3, paragraph [0008]). However, the dispersion device described in Patent Document 3 is designed for normal operation, in which powder is supplied to the stirring and mixing section together with dry gas and mixed with liquid, and the only locations that are subject to a dry gas atmosphere are those through which powder passes during normal operation, i.e., the powder supply section and the stirring and mixing section. Therefore, no consideration is given to locations where substances such as powder do not flow during normal operation.
上記特許文献4に記載される混合システムは、ドライガス供給部を備えたホッパーと混合機構とが外気と隔絶された状態で接続されていることから、液体や粉体などの材料が外気の水分と接触せずに混合することを可能としようとするものであり、これらの材料をドライガス環境に曝そうとするものである(段落〔0038〕、〔0044〕)等)。しかし、特許文献4に記載の混合システムも、装置の内部で複数の材料とドライガスとを共存させて混合するという通常運転時を前提としており、ドライガス環境とする対象箇所は、粉体が通常運転で通過する箇所、ホッパー及び混合機構だけである。そのため、特許文献4も、上記特許文献3と同様に、粉体等の物質が通常運転で流通しない箇所については、一切考慮されていない。 The mixing system described in Patent Document 4, above, has a hopper equipped with a dry gas supply unit and a mixing mechanism connected in a state isolated from the outside air, thereby attempting to mix materials such as liquids and powders without contacting moisture in the outside air and exposing these materials to a dry gas environment (paragraphs [0038], [0044], etc.). However, the mixing system described in Patent Document 4 also assumes normal operation, in which multiple materials and dry gas coexist and are mixed inside the device, and the only areas that are subject to a dry gas environment are the hopper and mixing mechanism, which are areas through which powder passes during normal operation. Therefore, like Patent Document 3, Patent Document 4 also makes no consideration whatsoever to areas where powder and other substances do not flow during normal operation.
本発明者らは、製造装置の運転開始、通常運転、運転停止及びメンテナンス作業等のあらゆる場面において発生する、上記物質の取扱いの手法、とりわけ移送の際に、物質と大気中の水分等との反応を極力抑制し、安全性を確保する手法について検討した。検討を進めた結果、移送用の装置として、窒素等の不活性ガスを貯蔵できる予備室を用いることに着目した。そして、このような予備室に不活性ガスを供給及び排出する機構を組み合わせ、かつ予備室を一の容器から他の容器への移送の際の物質が移送する移送用配管として用いることで、物質の移送に際して大気中の水分等との反応を極力抑制し得ることを見出した。 The inventors investigated methods for handling the above-mentioned substances, which arise in all situations, such as during the start-up, normal operation, shutdown, and maintenance of manufacturing equipment, and methods for ensuring safety, particularly during transfer, by minimizing reactions between the substances and moisture in the atmosphere. As a result of their investigation, they focused on using a spare chamber capable of storing an inert gas, such as nitrogen, as a transfer device. They then discovered that by combining such a spare chamber with a mechanism for supplying and discharging inert gas, and by using the spare chamber as a transfer pipe for transferring the substances when transferring them from one container to another, it is possible to minimize reactions between the substances and moisture in the atmosphere when transferring them.
一の容器から他の容器への移送の際に上記物質が流通するものの、通常運転では流通しない予備室を不活性ガス雰囲気とすること、また例えば一の容器に貯留される物質を他の容器に移送する際に、これらの一の容器と他の容器とを連結して行うような、通常運転とは異なる場面で使用する態様は、上記特許文献3及び4には一切記載されていない事柄である。 Patent documents 3 and 4 do not mention at all the following: the preliminary chamber, through which the substance flows when transferring from one container to another, is filled with an inert gas atmosphere; however, the preliminary chamber, through which the substance does not flow during normal operation; or the use of the system in situations other than normal operation, such as connecting one container to another when transferring a substance stored in one container to that other container.
また例えば、製造設備の稼働中に、上記物質が内部を通過する機器のメンテナンスする場合、予め内部を水等の流体を用いて洗浄することがあり、大気中の水分だけでなく、洗浄用に使用される水と、上記物質との反応が生じることがある。そして、洗浄に用いられた水は、機器の内部に滞留することがある。そのため、製造設備を運転停止した後、より安全かつ迅速にメンテナンスを行うには、機器の内部に滞留する洗浄に用いられた水をより効率的に除去することも重要となってくる。本発明者らは、このような場合、上記予備室と、不活性ガスの供給及び排出機構とを備え、予備室を物質の移送用配管として用いることで、機器の内部に滞留する洗浄に用いられた水をより効率的に除去することができ、その結果として、製造装置の稼働率の向上を図れるという、副次的な効果も得られることも見出した。
かくして、本発明の硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質の移送装置及び移送方法、並びに物質用機器の内部残留物の除去方法は、安全かつ効率的に、上記物質を取扱いし得るものとなった。
Furthermore, for example, when performing maintenance on equipment through which the above-mentioned substances pass during the operation of a manufacturing facility, the interior may be cleaned in advance with a fluid such as water. This may cause a reaction between the water used for cleaning and the above-mentioned substances, in addition to the moisture in the atmosphere. The water used for cleaning may then remain inside the equipment. Therefore, in order to perform maintenance more safely and quickly after shutting down the manufacturing facility, it is also important to more efficiently remove the water used for cleaning that remains inside the equipment. The inventors have discovered that in such cases, by providing the above-mentioned preliminary chamber and an inert gas supply and exhaust mechanism and using the preliminary chamber as a pipe for transferring the substances, the water used for cleaning that remains inside the equipment can be more efficiently removed, resulting in a secondary effect of improving the operating rate of the manufacturing equipment.
Thus, the transfer device and method of the present invention for a substance containing at least one atom selected from sulfur atoms and halogen atoms, as well as the method for removing internal residues from a substance-transporting device, can handle the above-mentioned substance safely and efficiently.
(本実施形態の各種形態について)
本実施形態の第一の形態に係る物質移送装置は、
硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質の移送装置であり、
移送用予備室と、移送物質入口部及び移送物質出口部と、不活性ガスの導入機構及び排出機構と、を備え、
前記移送物質入口部及び移送物質出口部は、前記移送用予備室に設けられ、かつ物質用第一容器の第一物質入口部及び第一物質出口部並びに物質用第二容器の第二物質移送口部と連結可能であり、
前記不活性ガスの導入機構は前記移送用予備室に不活性ガスを導入し、前記不活性ガスの排出機構は前記移送用予備室から不活性ガスを排出する、
物質移送装置、
である。
(Various aspects of this embodiment)
The substance transfer device according to the first aspect of this embodiment includes:
An apparatus for transferring a substance containing at least one atom selected from a sulfur atom and a halogen atom,
The apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism,
the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber;
material transfer equipment,
is.
本実施形態の第一の形態に係る物質移送装置によれば、例えば硫化リチウム、五硫化二リン、単体硫黄等の硫黄原子を含む物質、ハロゲン化リチウム、単体ハロゲン等のハロゲン原子を含む物質を第一容器から第二容器に(第二容器から第一容器であってもよい。)に物質を移送する際に、移送用予備室と、移送物質入口部及び移送物質出口部と、不活性ガスの導入機構及び排出機構と、を備えるという簡易な構造によって、当該物質と大気中の水分等との反応を抑制することで、安全性を確保することができる。また、安全性を確保することができることから、作業効率を向上させることが可能となる。その結果、安全かつ効率的に、硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質(以下、単に「物質」と称することがある。)を取扱いすることが可能となる。 In the material transfer device according to the first aspect of this embodiment, when transferring a material containing sulfur atoms, such as lithium sulfide, diphosphorus pentasulfide, or elemental sulfur, or a material containing halogen atoms, such as lithium halide or elemental halogen, from a first container to a second container (or from the second container to the first container), safety can be ensured by suppressing reactions between the material and moisture in the atmosphere, etc., with a simple structure that includes a transfer reserve chamber, a transfer material inlet and outlet, and an inert gas introduction and exhaust mechanism. Furthermore, because safety can be ensured, work efficiency can be improved. As a result, it becomes possible to safely and efficiently handle a material containing at least one atom selected from sulfur atoms and halogen atoms (hereinafter sometimes simply referred to as "material").
本実施形態の第二の形態に係る物質移送装置は、
前記不活性ガスの導入機構が、さらに前記物質用第一容器に設けられた不活性ガス導入口から不活性ガスを導入する、上記第一の形態に係る物質移送装置、
である。
A substance transfer device according to a second aspect of this embodiment includes:
The substance transfer apparatus according to the first aspect, wherein the inert gas introduction mechanism further introduces the inert gas from an inert gas inlet provided in the first substance container.
is.
不活性ガスの導入機構が、物質用第一容器に設けられた不活性ガス導入口から不活性ガスを導入することができることで、より安全かつ効率的に物質を取扱うことができる。また、後述する物質用容器の内部残留物の除去を行う場合に、より効率的に除去を行うことができることから、製造装置の稼働率の向上を図ることもできる。 The inert gas introduction mechanism can introduce inert gas through an inert gas inlet provided in the first substance container, allowing for safer and more efficient handling of substances. Furthermore, when removing internal residue from the substance container (described below), this can be done more efficiently, which can also improve the operating rate of the manufacturing equipment.
本実施形態の第三の形態に係る物質移送装置は、
前記移送用予備室が、筒状である、上記第一又は第二の形態に係る物質移送装置、
である。
A substance transfer device according to a third aspect of this embodiment includes:
The substance transfer apparatus according to the first or second aspect, wherein the transfer preliminary chamber is cylindrical.
is.
移送用予備室が筒状であると、安全性を担保しつつ、とりわけ物質の移送をより円滑に行うことができるため、より安全かつ効率的に物質を取扱いすることが可能となる。また、物質移送装置のメンテナンス性が向上する。 If the transfer pre-chamber is cylindrical, it is possible to ensure safety while, in particular, transferring materials more smoothly, making it possible to handle materials more safely and efficiently. It also improves the maintainability of the material transfer device.
本実施形態の第四の形態に係る物質移送装置は、
前記移送物質入口部及び移送物質出口部が、前記筒状である移送用予備室の両端に設けられる、上記第三の形態に係る物質移送装置、
である。
A substance transfer device according to a fourth aspect of this embodiment includes:
The substance transfer device according to the third aspect, wherein the transfer substance inlet portion and the transfer substance outlet portion are provided at both ends of the cylindrical transfer pre-chamber.
is.
このような簡易な構造を有することで、安全性を担保しつつ、とりわけ物質の移送をより円滑に行うことができるため、より安全かつ効率的に物質を取扱いすることが可能となる。また、物質移送装置のメンテナンス性が向上する。 Such a simple structure ensures safety while also enabling smoother material transfer, making it possible to handle materials more safely and efficiently. It also improves the maintainability of the material transfer device.
本実施形態の第五の形態に係る物質移送装置は、
前記不活性ガスの導入機構及び排出機構が、前記筒状である移送用予備室の側面に設けられる、上記第三又は第四の形態に係る物質移送装置、
である。
A substance transfer device according to a fifth aspect of this embodiment includes:
The substance transfer apparatus according to the third or fourth aspect, wherein the inert gas introduction mechanism and discharge mechanism are provided on a side surface of the cylindrical transfer pre-chamber.
is.
このような構造とすることで、より安定した不活性ガスの導入及び排出が可能となるため、安全性を担保しつつ、とりわけ物質の移送をより円滑に行うことができるので、より安全かつ効率的に物質を取扱いすることが可能となる。 This type of structure allows for more stable introduction and discharge of inert gas, ensuring safety and particularly facilitating smoother transfer of materials, making it possible to handle materials more safely and efficiently.
本実施形態の第六の形態に係る物質の移送方法は、
移送用予備室と、移送物質入口部及び移送物質出口部と、不活性ガスの導入機構及び排出機構と、を備え、
前記移送物質入口部及び移送物質出口部は、前記移送用予備室に設けられ、かつ物質用第一容器の第一物質入口部及び第一物質出口部並びに物質用第二容器の第二物質移送口部と連結可能であり、
前記不活性ガスの導入機構は前記移送用予備室に不活性ガスを導入し、前記不活性ガスの排出機構は前記移送用予備室から不活性ガスを排出する、
硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質の移送装置を用い、
下記(1A)~(3A)の操作を行う、物質の移送方法、
である。
(1A)前記移送物質入口部と前記物質用第一容器の物質出口部に設けられた弁1aとを連結し、前記移送物質出口部と前記物質用第二容器の第二物質移送口部に設けられた弁2とを連結する。
(2A)前記弁1a及び弁2を閉とし、前記不活性ガスの導入機構及び排出機構により不活性ガスの供給及び排出を行い、不活性ガスを前記移送用予備室に充填する。
(3A)前記不活性ガスの供給及び排出を停止し、前記弁1a及び弁2を開とし、前記物質用第一容器に貯留される物質を、前記物質用第二容器に移送する。
A method for transferring a substance according to a sixth aspect of the present embodiment includes:
The apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism,
the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber;
using a transfer device for a substance containing at least one atom selected from a sulfur atom and a halogen atom,
A method for transferring a substance, comprising the steps of (1A) to (3A) below:
is.
(1A) The transfer substance inlet portion is connected to a valve 1a provided at the substance outlet portion of the first substance container, and the transfer substance outlet portion is connected to a valve 2 provided at the second substance transfer port portion of the second substance container.
(2A) The valves 1a and 2 are closed, and the inert gas is supplied and discharged by the inert gas introduction mechanism and discharge mechanism, filling the inert gas into the transfer preliminary chamber.
(3A) The supply and discharge of the inert gas are stopped, the valves 1a and 2 are opened, and the substance stored in the first substance container is transferred to the second substance container.
本実施形態の物質の移送方法は、上記本実施形態の物質移送装置を採用するものである。そして、本実施形態の物質移送装置において上記(1A)~(3A)の手順で操作を行うことで、安全性を担保しつつ、とりわけ物質の移送をより円滑に行うことができるため、安全かつ効率的に物質を取扱いすることが可能となる。 The material transfer method of this embodiment employs the material transfer device of this embodiment described above. By performing the operations of the material transfer device of this embodiment in accordance with the steps (1A) to (3A) above, safety can be ensured while particularly material transfer can be carried out more smoothly, making it possible to handle materials safely and efficiently.
本実施形態の第七の形態に係る物質の移送方法は、
前記(3A)に次いで、前記(2A)、下記(4A)及び(5A)の操作を行う、上記第六の形態に係る物質の移送方法、
である。
(4A)前記物質用第二容器及び弁2を前記移送物質出口部から取り外す。
(5A)前記移送物質出口部に、閉止フランジを取り付ける。
A substance transfer method according to a seventh aspect of the present embodiment includes:
The method for transferring a substance according to the sixth aspect, comprising carrying out the operations (2A) and (4A) and (5A) below after the operation (3A);
is.
(4A) The second substance container and valve 2 are removed from the transfer substance outlet.
(5A) A closing flange is attached to the outlet portion of the transfer substance.
(3A)の操作に次いで、上記(2A)、(4A)及び(5A)の操作を順に行うことで、安全性を担保しつつ、とりわけ物質の移送をより円滑に行うことができるため、より安全かつ効率的に物質を取扱いすることが可能となる。 By performing the above operations (2A), (4A), and (5A) in order following operation (3A), safety can be ensured while, in particular, the transfer of substances can be carried out more smoothly, making it possible to handle substances more safely and efficiently.
本実施形態の第八の形態に係る物質用容器の内部残留物の除去方法は、
移送用予備室と、移送物質入口部及び移送物質出口部と、不活性ガスの導入機構及び排出機構と、を備え、
前記移送物質入口部及び移送物質出口部は、前記移送用予備室に設けられ、かつ物質用第一容器の第一物質入口部及び第一物質出口部並びに物質用第二容器の第二物質移送口部と連結可能であり、
前記不活性ガスの導入機構は前記移送用予備室に不活性ガスを導入し、前記不活性ガスの排出機構は前記移送用予備室から不活性ガスを排出する、
硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質の移送装置を用い、
下記(1B)及び(2B)の操作を行う、物質用容器の内部残留物の除去方法、
である。
(1B)前記移送物質入口部と前記物質用第一容器の物質出口部に設けられた弁1aとを連結する。
(2B)前記弁1aを開とし、前記不活性ガスの導入機構及び排出機構により不活性ガスの供給及び排出を行い、不活性ガスを前記移送用予備室及び前記物質用第一容器に充填する。
A method for removing internal residue from a substance container according to an eighth aspect of this embodiment includes:
The apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism,
the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber;
using a transfer device for a substance containing at least one atom selected from a sulfur atom and a halogen atom,
A method for removing internal residues from a substance container, comprising the steps of (1B) and (2B) below:
is.
(1B) The transfer substance inlet is connected to the valve 1a provided at the substance outlet of the first substance container.
(2B) The valve 1a is opened, and the inert gas is supplied and discharged by the inert gas introduction mechanism and discharge mechanism, filling the inert gas into the transfer pre-chamber and the first substance container.
既述のように、機器のメンテナンスを行う際に、予め内部を水等の流体を用いて洗浄することがあり、大気中の水分だけでなく、洗浄用に使用される水と、上記物質との反応が生じることがある。このように、洗浄に用いられた水等の媒体、また物質自体も、機器の内部に滞留することがある。
本実施形態の物質用容器の内部残留物の除去方法は、上記本実施形態の物質移送装置を採用するものである。そして、本実施形態の物質移送装置において上記(1B)~(2B)の手順で操作を行うことで、安全性を担保しつつ、とりわけ機器(物質用容器)の内部残留物の除去をより円滑に行うことができるため、安全かつ効率的に物質を取扱いすることが可能となる。さらに、物質用容器の内部残留物の除去をより円滑に行うことは、物質用容器内の不活性ガスによるパージを行うこととなり、メンテナンス後の製造装置の運転開始をより迅速に行うことができるので、製造装置の稼働率の向上を図ることにもつながる。
As mentioned above, when performing maintenance on equipment, the inside of the equipment may be washed with a fluid such as water beforehand, and this may cause a reaction between not only the moisture in the air but also the water used for washing and the above-mentioned substances. In this way, the medium such as water used for washing, as well as the substances themselves, may remain inside the equipment.
The method for removing internal residue from a substance container of this embodiment employs the substance transfer apparatus of this embodiment. By performing the procedures (1B) to (2B) above with the substance transfer apparatus of this embodiment, it is possible to ensure safety and, in particular, more smoothly remove internal residue from the equipment (substance container), thereby enabling safe and efficient substance handling. Furthermore, more smoothly removing internal residue from a substance container involves purging the substance container with an inert gas, which allows for more rapid start-up of the manufacturing equipment after maintenance, thereby improving the operating rate of the manufacturing equipment.
本実施形態の第九の形態に係る物質用容器の内部残留物の除去方法は、
前記不活性ガスの導入機構により、前記物質用第一容器に設けられた不活性ガス導入口より不活性ガスを導入する、上記第八の形態に係る物質用容器の内部残留物の除去方法、
である。
A method for removing internal residue from a substance container according to a ninth aspect of this embodiment includes:
the inert gas introduction mechanism introduces an inert gas from an inert gas inlet provided in the first container for the substance;
is.
弁1a及び移送用予備室を介して不活性ガスを導入するだけでなく、さらに物質用第一容器から不活性ガスを導入することで、より効率的に物質用容器の内部残留物を除去することが可能となる。その結果、より安全かつ効率的に物質を取扱いすることができ、製造装置の稼働率の向上を図ることもできる。 In addition to introducing inert gas via valve 1a and the transfer auxiliary chamber, introducing inert gas from the first substance container also makes it possible to more efficiently remove internal residue from the substance container. As a result, substances can be handled more safely and efficiently, and the operating rate of the manufacturing equipment can also be improved.
〔物質移送装置〕
本実施形態の物質移送装置は、
硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質の移送装置であり、
移送用予備室と、移送物質入口部及び移送物質出口部と、不活性ガスの導入機構及び排出機構と、を備え、
前記移送物質入口部及び移送物質出口部は、前記移送用予備室に設けられ、かつ物質用第一容器の第一物質入口部及び第一物質出口部並びに物質用第二容器の第二物質移送口部と連結可能であり、
前記不活性ガスの導入機構は前記移送用予備室に不活性ガスを導入し、前記不活性ガスの排出機構は前記移送用予備室から不活性ガスを排出する、
という装置である。
[Matter transfer device]
The substance transfer device of this embodiment is
An apparatus for transferring a substance containing at least one atom selected from a sulfur atom and a halogen atom,
The apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism,
the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber;
This is the device.
(硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質)
本実施形態の物質移送装置における移送の対象物としては、硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質であれば特に制限なく該当する。
例えば、本実施形態の物質移送装置が好適に用いられる硫化物固体電解質の製造装置において、硫黄原子を含む物質としては、硫黄原子を含む固体電解質原料;錯化剤を使用する場合は電解質前駆体、耐圧容器を使用する場合は耐圧容器を用いて溶媒中で熱処理した熱処理物等の中間体;製品となる硫化物固体電解質;等が挙げられる。
(Substances containing at least one atom selected from sulfur atoms and halogen atoms)
The substance to be transferred in the substance transfer device of this embodiment is not particularly limited as long as it contains at least one atom selected from sulfur atoms and halogen atoms.
For example, in a sulfide solid electrolyte production apparatus in which the substance transfer device of the present embodiment is suitably used, examples of the substance containing sulfur atoms include a solid electrolyte raw material containing sulfur atoms; an electrolyte precursor when a complexing agent is used, an intermediate such as a heat-treated product obtained by heat treatment in a solvent using a pressure-resistant container when a pressure-resistant container is used; and a sulfide solid electrolyte that will be the product.
ハロゲン原子を含む物質としては、ハロゲン原子を含む固体電解質原料;錯化剤を使用する場合は電解質前駆体、耐圧容器を使用する場合は耐圧容器を用いて熱処理した熱処理物等の中間体;製品となる硫化物固体電解質;等が挙げられる。また、硫黄原子及びハロゲン原子を含む物質としては、上記硫黄原子を含む固体電解質原料及びハロゲン原子を含む固体電解質原料を用いて得られる電解質前駆体及び熱処理物等の中間体;製品となる硫化物固体電解質;等が挙げられる。これらの固体電解質原料、中間体及び硫化物固体電解質の詳細については、後述する。 Examples of substances containing halogen atoms include solid electrolyte raw materials containing halogen atoms; electrolyte precursors when a complexing agent is used, intermediates such as heat-treated products obtained by heat treatment using a pressure-resistant vessel when a pressure-resistant vessel is used; and sulfide solid electrolyte products that will be the product. Furthermore, examples of substances containing sulfur atoms and halogen atoms include intermediates such as electrolyte precursors and heat-treated products obtained using the above-mentioned solid electrolyte raw materials containing sulfur atoms and solid electrolyte raw materials containing halogen atoms; and sulfide solid electrolyte products that will be the product. Details of these solid electrolyte raw materials, intermediates, and sulfide solid electrolytes will be provided below.
硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質は、既述のように固体電解質原料、中間体及び硫化物固体電解質であり、基本的には粉体であるが、液体であってもよく、また粉体を含むスラリー状であってもよい。 As already mentioned, substances containing at least one atom selected from sulfur atoms and halogen atoms are solid electrolyte raw materials, intermediates, and sulfide solid electrolytes, and are basically in the form of powder, but may also be in the form of a liquid or a slurry containing powder.
(固体電解質原料)
上記硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質となる固体電解質原料としては例えば硫化リチウム;フッ化リチウム、塩化リチウム、臭化リチウム、ヨウ化リチウム等のハロゲン化リチウム;三硫化二リン(P2S3)、五硫化二リン(P2S5)等の硫化リン;臭素(Br2)、ヨウ素(I2)等のハロゲン単体;硫黄単体等が代表的に挙げられる。また、PS4構造を含むLi3PS4を固体電解質原料として用いることもできる。
これらの例示した固体電解質原料は、固体(粉体)状又は液体状である。
(Solid electrolyte raw material)
Representative examples of the solid electrolyte raw material containing at least one atom selected from the sulfur atom and the halogen atom include lithium sulfide; lithium halides such as lithium fluoride, lithium chloride, lithium bromide, and lithium iodide; phosphorus sulfides such as phosphorus trisulfide ( P2S3 ) and phosphorus pentasulfide ( P2S5 ); elemental halogens such as bromine ( Br2 ) and iodine ( I2 ); and elemental sulfur. Li3PS4 , which has a PS4 structure, can also be used as the solid electrolyte raw material.
These exemplified solid electrolyte raw materials are in solid (powder) or liquid form.
(中間体)
中間体としては、例えば上記の硫黄原子を含む固体電解質原料及びハロゲン原子を含む固体電解質原料を用いて得られる電解質前駆体、及び耐圧容器を使用する場合は耐圧容器を用いて熱処理した熱処理物等が代表的に挙げられる。
電解質前駆体は、固体電解質原料と、窒素原子、酸素原子、塩素原子等のハロゲン原子、硫黄原子等のヘテロ原子を含む溶媒(「錯化剤」とも称される。)と、の混合により生成する、固体電解質原料と錯化剤との結合により生じる錯体を意味する。これらのヘテロ原子は、リチウム原子との親和性が高いことから、錯体が生じる。固体電解質原料と錯化剤との結合により生じる錯体は、これを加熱乾燥することで、錯体を構成するヘテロ原子を含む溶媒が除去され、固体電解質が生成することから、電解質前駆体と称される。
(Intermediate)
Representative examples of the intermediate include an electrolyte precursor obtained using the above-mentioned solid electrolyte raw material containing a sulfur atom and a solid electrolyte raw material containing a halogen atom, and a heat-treated product obtained by heat treatment using a pressure-resistant container when a pressure-resistant container is used.
The term "electrolyte precursor" refers to a complex formed by the combination of a solid electrolyte raw material and a solvent (also referred to as a "complexing agent") containing heteroatoms such as nitrogen atoms, oxygen atoms, halogen atoms (e.g., chlorine atoms), and sulfur atoms. These heteroatoms have a high affinity for lithium atoms, resulting in the formation of a complex. The complex formed by the combination of the solid electrolyte raw material and the complexing agent is heated and dried to remove the solvent containing the heteroatoms that make up the complex, thereby producing a solid electrolyte, hence the term "electrolyte precursor."
耐圧容器を用いて熱処理した熱処理物は、より具体的には、好ましくは上記固体電解質原料を必要に応じて粉砕処理し、得られた粉砕処理物を、必要に応じて粗混合し、さらに溶媒中で混合粉砕して得られた固体電解質混合物を、耐圧容器を用いて熱処理して得られるものである。ここで、溶媒としては、炭化水素溶媒等の非極性溶媒を用いればよく、好ましくは更にニトリル化合物及びエーテル化合物から選ばれる少なくとも一の極性溶媒を用いることが好ましい。 More specifically, the heat-treated product obtained by heat treatment using a pressure-resistant vessel is preferably obtained by pulverizing the above-mentioned solid electrolyte raw material as needed, coarsely mixing the resulting pulverized product as needed, and then mixing and pulverizing the resulting solid electrolyte mixture in a solvent, followed by heat treatment using a pressure-resistant vessel. The solvent used here may be a non-polar solvent such as a hydrocarbon solvent, and preferably also at least one polar solvent selected from nitrile compounds and ether compounds.
熱処理の条件は、加熱温度として好ましくは150~300℃、より好ましくは160~280℃である。
このようにして得られる熱処理物は、焼成することでアルジロダイト型固体電解質が得られることから、中間体と称し得るものである。
The heat treatment is carried out at a heating temperature of preferably 150 to 300°C, more preferably 160 to 280°C.
The heat-treated product thus obtained can be called an intermediate because an argyrodite-type solid electrolyte can be obtained by firing it.
(硫化物固体電解質)
硫化物固体電解質としては、例えば上記電解質前駆体から錯化剤を除去することで、また上記熱処理物を焼成することで、得られるものである。硫化物固体電解質としては、後述する非晶性硫化物固体電解質、結晶性硫化物固体電解質が挙げられる。
(Sulfide solid electrolyte)
The sulfide solid electrolyte can be obtained, for example, by removing the complexing agent from the electrolyte precursor or by firing the heat-treated product. Examples of the sulfide solid electrolyte include an amorphous sulfide solid electrolyte and a crystalline sulfide solid electrolyte, which will be described later.
非晶性硫化物固体電解質として代表的なものとしては、例えば、Li2S-P2S5、Li2S-P2S5-LiI、Li2S-P2S5-LiCl、Li2S-P2S5-LiBr、Li2S-P2S5-LiI-LiBr等の硫化リチウムと硫化リンとハロゲン化リチウムとから構成される硫化物固体電解質;更に酸素原子、珪素原子等の他の原子を含む、例えば、Li2S-P2S5-Li2O-LiI、Li2S-P2S5-Li2O-LiI-LiBr、Li2S-SiS2-P2S5-LiI等の硫化物固体電解質が好ましく挙げられる。
非晶性硫化物固体電解質を構成する原子の種類は、例えば、ICP発光分光分析装置により確認することができる。
Representative examples of amorphous sulfide solid electrolytes include sulfide solid electrolytes composed of lithium sulfide , phosphorus sulfide , and lithium halide, such as Li 2 S—P 2 S 5 , Li 2 S—P 2 S 5 -LiI, Li 2 S—P 2 S 5 -LiCl, Li 2 S—P 2 S 5 -LiBr, and Li 2 S—P 2 S 5 -LiI-LiBr; and sulfide solid electrolytes further containing other atoms such as oxygen atoms and silicon atoms, such as Li 2 S—P 2 S 5 -Li 2 O—LiI, Li 2 S—P 2 S 5 -Li 2 O—LiI-LiBr, and Li 2 S—SiS 2 -P 2 S 5 Preferred examples of the solid electrolyte include sulfide solid electrolytes such as LiI.
The types of atoms constituting the amorphous sulfide solid electrolyte can be confirmed, for example, by an ICP emission spectrometer.
結晶性硫化物固体電解質は、非晶質硫化物固体電解質を結晶化温度以上に加熱して得られる、いわゆるガラスセラミックスであってもよく、その結晶構造としては、Li3PS4結晶構造、Li4P2S6結晶構造、Li7PS6結晶構造、Li7P3S11結晶構造、2θ=20.2°近傍及び23.6°近傍にピークを有する結晶構造(例えば、特開2013-16423号公報)等が挙げられる。 The crystalline sulfide solid electrolyte may be a so-called glass ceramic obtained by heating an amorphous sulfide solid electrolyte to a temperature equal to or higher than the crystallization temperature, and examples of the crystal structure include a Li 3 PS 4 crystal structure, a Li 4 P 2 S 6 crystal structure, a Li 7 PS 6 crystal structure, a Li 7 P 3 S 11 crystal structure, and a crystal structure having peaks at 2θ=approximately 20.2° and 23.6° (for example, JP 2013-16423 A).
また、Li4-xGe1-xPxS4系チオリシコンリージョンII(thio-LISICON Region II)型結晶構造(Kannoら、Journal of The Electrochemical Society,148(7)A742-746(2001)参照)、Li4-xGe1-xPxS4系チオリシコンリージョンII(thio-LISICON Region II)型と類似の結晶構造(Solid State Ionics,177(2006),2721-2725参照)等も挙げられる。 Other examples include a Li 4-x Ge 1-x P x S 4 based thio-LISICON Region II type crystal structure (see Kanno et al., Journal of The Electrochemical Society, 148(7)A742-746(2001)), a crystal structure similar to a Li 4-x Ge 1-x P x S 4 based thio-LISICON Region II type (see Solid State Ionics, 177(2006), 2721-2725), and the like.
また上記のLi7PS6の構造骨格を有し、Pの一部をSiで置換してなるアルジロダイト型結晶構造を有する結晶性硫化物固体電解質も好ましく挙げられる。
アルジロダイト型結晶構造の組成式としては、例えば組成式Li7-xP1-ySiyS6及びLi7+xP1-ySiyS6(xは-0.6~0.6、yは0.1~0.6)で示される結晶構造、また アルジロダイト型結晶構造の組成式としては、組成式Li7-x-2yPS6-x-yClx(0.8≦x≦1.7、0<y≦-0.25x+0.5)も挙げられる。
Another preferred example is a crystalline sulfide solid electrolyte having the above-mentioned Li 7 PS 6 structural skeleton and an argyrodite-type crystal structure in which part of the P is substituted with Si.
Examples of the composition formula of the argyrodite-type crystal structure include the crystal structures represented by the composition formula Li 7-x P 1-y Si y S 6 and Li 7+x P 1-y Si y S 6 (x is −0.6 to 0.6, y is 0.1 to 0.6), and the composition formula of the argyrodite-type crystal structure also includes the composition formula Li 7-x-2y PS 6-x-y Cl x (0.8≦x≦1.7, 0<y≦−0.25x+0.5).
(用途)
本実施形態の物質移送装置は、既述のように硫化物固体電解質の製造装置において好適に用いられる。具体的には、硫化物固体電解質の製造装置を構成する機器であって、製造装置の稼働中に内部を硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質が流通する機器、また当該物質を貯蔵する物質用容器等に連結して用いられる。
(Application)
The substance transfer device of this embodiment is suitable for use in a sulfide solid electrolyte production apparatus, as described above. Specifically, the substance transfer device is used by connecting to a component of the sulfide solid electrolyte production apparatus, through which a substance containing at least one atom selected from sulfur atoms and halogen atoms flows during operation of the production apparatus, or to a substance container for storing the substance.
本実施形態の物質移送装置を連結して用いる場合の、連結先となる硫化物固体電解質の製造装置を構成する機器としては、硫化物固体電解質の製造方法に応じてかわり得るが、主に固体電解質原料の反応に用いられる反応機器;溶媒(錯化剤を含む)を用いる場合は、固体電解質原料及び/又は電解質前駆体等の中間体並びに溶媒(錯化剤を含む)を含むスラリー又は溶液から溶媒(錯化剤を含む)を除去するための加熱機器;結晶化等のための加熱機器;硫化物固体電解質を分離する分離機器;硫化物固体電解質の粒径を調整するための粒度調整機器;また耐圧容器を用いて熱処理する場合は耐圧容器、当該熱処理物を焼成する加熱機器;これらの機器を連結する配管;上記物質を貯蔵する物質用容器;などが主に挙げられる。これらの機器については、硫化物固体電解質の製造方法及び製造装置の説明にて詳述する。 When the material transfer apparatus of this embodiment is used in a connected manner, the equipment constituting the sulfide solid electrolyte production apparatus to which it is connected may vary depending on the sulfide solid electrolyte production method, but mainly includes reaction equipment used for reacting the solid electrolyte raw materials; when a solvent (including a complexing agent) is used, heating equipment for removing the solvent (including a complexing agent) from a slurry or solution containing the solid electrolyte raw materials and/or intermediates such as an electrolyte precursor and the solvent (including a complexing agent); heating equipment for crystallization, etc.; separation equipment for separating the sulfide solid electrolyte; particle size adjustment equipment for adjusting the particle size of the sulfide solid electrolyte; when heat treatment is performed using a pressure-resistant container, heating equipment for firing the pressure-resistant container and the heat-treated product; piping connecting these devices; and material containers for storing the above-mentioned materials. These devices will be described in detail in the description of the sulfide solid electrolyte production method and production apparatus.
(物質移送装置の構成)
本実施形態の物質移送装置の構成について、図1を用いて説明する。
図1には、本実施形態の物質移送装置が、移送用予備室と、移送物質入口部及び移送物質出口部と、不活性ガスの導入機構及び排出機構と、を備えていることが示されている。図1において「B/L」(「バッテリーリミット」の略語である。)と示されている境界線に囲まれる内側が、本実施形態の物質移送装置の範囲に該当する。
(Configuration of material transfer device)
The structure of the substance transfer device of this embodiment will be described with reference to FIG.
1 shows that the substance transfer device of this embodiment is equipped with a transfer preliminary chamber, a transfer substance inlet and outlet ports, and an inert gas introduction mechanism and exhaust mechanism. The area enclosed by the boundary line indicated as "B/L" (abbreviation for "battery limit") in FIG. 1 corresponds to the range of the substance transfer device of this embodiment.
物質移送装置の移送物質入口部及び移送物質出口部は、移送用予備室に設けられており、図1に示されるように移送用予備室の両端に設けられていることが好ましい。また、物質移送装置の移送物質入口部及び移送物質出口部は、物質用第一容器の第一物質入口部及び第一物質出口部並びに物質用第二容器の第二物質移送口部と連結可能であり、図1では各々物質用第一容器の第一物質出口部及び物質用第二容器の第二物質移送口部と連結しており、本実施形態の物質移送装置は、物質用第一容器と物質用第二容器とを連結するように設けられていることが示されている。 The transfer substance inlet and outlet ports of the substance transfer device are provided in the transfer preparation chamber, and are preferably provided at both ends of the transfer preparation chamber as shown in Figure 1. Furthermore, the transfer substance inlet and outlet ports of the substance transfer device can be connected to the first substance inlet and first substance outlet ports of the first substance container and the second substance transfer port of the second substance container; in Figure 1 they are connected to the first substance outlet port of the first substance container and the second substance transfer port of the second substance container, respectively, and the substance transfer device of this embodiment is shown as being configured to connect the first substance container and the second substance container.
不活性ガスの導入機構及び排出機構は、移送用予備室に設けられ、不活性ガスを移送用予備室に導入し、排出し得ることが図1に示されている。また、図1には、好ましい態様として、不活性ガスの導入機構が、さらに物質用第一容器に設けられた不活性ガス導入口から不活性ガスを導入することが示されている。 FIG. 1 shows that the inert gas introduction mechanism and exhaust mechanism are provided in the transfer pre-chamber, and can introduce and exhaust the inert gas into the transfer pre-chamber. FIG. 1 also shows that, in a preferred embodiment, the inert gas introduction mechanism further introduces the inert gas from an inert gas inlet provided in the first substance container.
図1においては、物質用第一容器に貯留される物質を、物質用第二容器に移動する態様が示されている。図1に示されるように、物質の移送は、自重によって行われることが好ましい。 In Figure 1, a manner in which a substance stored in a first substance container is transferred to a second substance container is shown. As shown in Figure 1, the substance is preferably transferred by gravity.
図1には、物質用第一容器が「第一物質入口部(出口部)」、「第一物質出口部(入口部)」を有することが記載されている。これは、第一物質入口部は、本実施形態の物質移送装置の使用態様によっては第一物質出口部になり得、他方第一物質出口部は第一物質入口部になり得ることを意味する。既述のように、図1では、物質用第一容器に貯留される物質を、物質用第二容器に移送する態様が示されているが、これとは逆に、物質用第二容器に貯留される物質を、物質用第一容器に移送する場合、すなわち物質用第二容器に貯留される物質を自重で物質用第一容器に移送する場合、第一物質入口部は第一物質出口部となり、第一物質出口部は第一物質入口部となる。 In Figure 1, it is stated that the first substance container has a "first substance inlet portion (outlet portion)" and a "first substance outlet portion (inlet portion)." This means that the first substance inlet portion can become the first substance outlet portion depending on the manner in which the substance transfer device of this embodiment is used, and the first substance outlet portion can become the first substance inlet portion. As mentioned above, in Figure 1, an embodiment is shown in which a substance stored in the first substance container is transferred to the second substance container. However, conversely, when a substance stored in the second substance container is transferred to the first substance container, i.e., when a substance stored in the second substance container is transferred to the first substance container under its own weight, the first substance inlet portion becomes the first substance outlet portion, and the first substance outlet portion becomes the first substance inlet portion.
また、図1には、本実施形態の物質移送装置の移送物体入口部と物質用第一容器の第一物質出口部との間に弁1aが設けられ、本実施形態の物質移送装置の移送物体出口部と物質用第二容器の第二物質移送口部との間に弁2が設けられていることが示されている。これらの弁は、本実施形態の物質移送装置と、物質用第一容器及び物質用第二容器と、を仕切るために設けられる弁であり、物質を物質用第一容器と物質用第二容器との間で移送する際に使用される。これらの弁は、図1に示されるように物質用第一容器及び物質用第二容器に備えられる弁であってもよいし、また本実施形態の物質移送装置が備える弁であってもよい。 Furthermore, Figure 1 shows that a valve 1a is provided between the transfer object inlet port of the material transfer device of this embodiment and the first material outlet port of the first material container, and a valve 2 is provided between the transfer object outlet port of the material transfer device of this embodiment and the second material transfer port of the second material container. These valves are provided to separate the material transfer device of this embodiment from the first material container and the second material container, and are used when transferring material between the first material container and the second material container. These valves may be valves provided in the first material container and the second material container as shown in Figure 1, or may be valves provided in the material transfer device of this embodiment.
(移送用予備室)
移送用予備室は、物質用第一容器と物質用第二容器との間で物質を移送する際に、物質が通過するための流路である。また、状況に応じて物質を一時的に貯留するためにも用いられる。
(Transportation spare room)
The transfer chamber is a flow path through which the substance passes when transferring the substance between the first and second substance containers, and can also be used to temporarily store the substance depending on the situation.
移送用予備室の形態としては、移送用予備室内を物質が通過できる形態であり、不活性ガスの導入機構及び排出機構を設けることができれば特に制限はなく、配管状の場合の断面形状としては、好ましくは後述する物質用第一容器の第一物質入口部及び第一物質出口部、並びに物質用第二容器の第二物質移送口部の断面形状と同じであることが好ましく、例えば円、楕円、長方形、正方形等が好ましく挙げられ、より好ましくは円、楕円、更に好ましくは円である。すなわち、移送用予備室の形状は筒状であることが好ましい。筒状としては、より具体的には円柱、楕円柱、角柱が好ましく挙げられ、円柱、楕円柱がより好ましく、円柱が更に好ましい。このような形状とすることで、物質の移送の際に、移送用予備室内に物質が滞留しにくくなり、より円滑に物質の移送を行うことができる。 The shape of the transfer pre-chamber is not particularly limited as long as it allows the substance to pass through it and can be provided with an inert gas introduction mechanism and exhaust mechanism. When it is piping-shaped, the cross-sectional shape is preferably the same as the cross-sectional shapes of the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container, which will be described later. Preferred shapes include circle, ellipse, rectangle, and square, with circle and ellipse being more preferred, and circle being even more preferred. That is, the shape of the transfer pre-chamber is preferably cylindrical. More specifically, preferred cylindrical shapes include a cylinder, elliptical cylinder, and rectangular cylinder, with cylinder and elliptical cylinder being more preferred, and cylinder being even more preferred. By using such a shape, the substance is less likely to remain in the transfer pre-chamber during substance transfer, allowing for smoother substance transfer.
移送用予備室の形状が筒状である場合、移送用予備室は例えば配管により構成することができる。配管により構成することで、本実施形態の物質移送装置を所望の大きさ及び形状に調整しやすくなり、物質の移送の際に、移送用予備室内に物質が滞留しにくくなり、より円滑に物質の移送を行うことができる。
また、移送用予備室の形状について、所望の形状に応じて決定することができ、例えば筒状とする場合(配管により構成する場合)、直線形状(直線配管)、蛇行形状(蛇行配管)とすることができ、物質の移送の際に、移送用予備室内に物質が滞留しにくくなり、より円滑に物質の移送を行うことを考慮すると、直線形状(直線配管)とすることが好ましい。
When the preliminary transfer chamber is cylindrical, the preliminary transfer chamber can be configured, for example, by piping. By configuring the preliminary transfer chamber by piping, the substance transfer device of this embodiment can be easily adjusted to a desired size and shape, and the substance is less likely to remain in the preliminary transfer chamber during substance transfer, allowing for smoother substance transfer.
Furthermore, the shape of the transfer pre-chamber can be determined according to the desired shape; for example, if it is cylindrical (when constructed from piping), it can be linear (straight piping), or serpentine (serpentine piping). Considering that this makes it less likely for the substance to remain in the transfer pre-chamber when transferring the substance and allows for smoother transfer of the substance, a linear shape (straight piping) is preferable.
移送用予備室の断面形状の大きさについても、上記断面形状と同様に、後述する物質用第一容器の第一物質入口部及び第一物質出口部、並びに物質用第二容器の第二物質移送口部の大きさと同じであることが好ましい。移送用予備室が筒状である場合、断面形状の直径(内径)として通常5mm以上310mm以下とすればよく、好ましくは10mm以上、より好ましくは20mm以上であり、上限として好ましくは260mm以下、より好ましくは220mm以下である。移送用予備室を配管により構成する場合、配管のサイズとして通常1/4インチ以上12インチ以下であり、好ましくは1/2インチ以上、より好ましくは1インチ以上であり、上限として好ましくは10インチ以下、より好ましくは8・1/2インチ以下である。 The size of the cross-sectional shape of the transfer pre-chamber, like the above cross-sectional shape, is preferably the same as the size of the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container, described below. When the transfer pre-chamber is cylindrical, the diameter (inner diameter) of the cross-sectional shape is typically 5 mm or more and 310 mm or less, preferably 10 mm or more, more preferably 20 mm or more, with an upper limit of preferably 260 mm or less, more preferably 220 mm or less. When the transfer pre-chamber is constructed using piping, the size of the piping is typically 1/4 inch or more and 12 inches or less, preferably 1/2 inch or more, more preferably 1 inch or more, with an upper limit of preferably 10 inches or less, more preferably 8.5 inches or less.
移送用予備室の形状について、長さとしては不活性ガスの導入機構及び排出機構を設けることができれば特に制限はなく、設置する箇所等に応じて決定すればよいので一概にはいえないが、配管部分の長さとして、通常10cm以上1m以下とすればよい。 Regarding the shape of the transfer pre-chamber, there are no particular restrictions on its length as long as it can accommodate an inert gas introduction and exhaust mechanism, and it can be determined depending on the installation location, etc., so it is difficult to generalize, but the length of the piping portion should usually be between 10 cm and 1 m.
(移送物質入口部及び移送物質出口部)
移送用予備室に設けられる移送物質入口部及び移送物質出口部は、物質用第一容器の第一物質入口部及び第一物質出口部並びに物質用第二容器の第二物質移送口部と連結可能であれば特に制限はなく、例えば移送用予備室が筒状である場合(配管により構成する場合)、図1に示されるように、筒状(配管)の両端に設けられることが好ましい。物質用第一容器及び物質用第二容器との連結がより容易となるため、本実施形態の物質移送装置の利便性が向上する。
(Transferred substance inlet and outlet)
The transfer substance inlet and outlet provided in the preliminary transfer chamber are not particularly limited as long as they can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container, and for example, when the preliminary transfer chamber is cylindrical (configured by piping), it is preferable that they be provided at both ends of the cylinder (piping) as shown in Figure 1. This makes it easier to connect the first substance container and the second substance container, improving the convenience of the substance transfer device of this embodiment.
移送用予備室に設けられる移送物質入口部及び移送物質出口部は、物質用第一容器及び物質用第二容器との連結をより容易とし、利便性を向上させるため、物質用第一容器の第一物質入口部及び第一物質出口部並びに物質用第二容器の第二物質移送口部の形式に対応する形式を採用することが好ましい。例えば、フランジ、ねじ込み等の配管継手で採用される連結形式とすることが好ましい。これらの方式とすることで、本実施形態の物質移送装置の、上記第一物質入口部及び第一物質出口部並びに第二物質移送口部との着脱が容易となるため、利便性が向上する。また、図1に示されるように、必要に応じて弁1a及び弁2等の仕切り弁(図1参照)が採用される場合、これらの弁との着脱が容易になるため、利便性が向上する。 In order to facilitate easier connection to the first and second substance containers and improve convenience, the transfer substance inlet and outlet ports provided in the transfer preparation chamber preferably adopt a format that corresponds to the format of the first substance inlet and outlet ports of the first substance container and the second substance transfer port of the second substance container. For example, a connection format using a piping joint such as a flange or threaded joint is preferable. By adopting such a format, the first substance inlet and outlet ports and second substance transfer port of the substance transfer device of this embodiment can be easily attached and detached, improving convenience. Furthermore, as shown in Figure 1, if gate valves such as valve 1a and valve 2 (see Figure 1) are used as needed, attachment and detachment to these valves becomes easier, improving convenience.
(不活性ガスの導入機構及び排出機構)
不活性ガスの導入機構は、不活性ガスを移送用予備室に導入できればよく、その他特に制限はなく、例えば図1に示されるように、不活性ガスの供給源より不活性ガスを受け入れる連結部、当該連結部から移送用予備室への配管及び当該配管内の仕切り弁を備えていることが好ましい。仕切り弁を備えることで、後述する移送方法をより容易に行うことが可能となり、利便性が向上する。
(Inert gas introduction mechanism and exhaust mechanism)
The inert gas introduction mechanism is not particularly limited as long as it can introduce the inert gas into the transfer preparatory chamber, and preferably includes, for example, a connection part for receiving the inert gas from an inert gas supply source, a pipe from the connection part to the transfer preparatory chamber, and a gate valve in the pipe, as shown in Fig. 1. By including the gate valve, the transfer method described below can be performed more easily, improving convenience.
不活性ガスの導入機構は、図1に示されるように、移送用予備室が筒状である場合、その側面に設けられることが好ましい。より具体的には、不活性ガスを、連結部から移送用予備室に供給するための配管は、移送用予備室の側面に接続されていることが好ましい。このように接続されていることで、より安定した不活性ガスの導入が可能となるため、安全性を担保しつつ、とりわけ物質の移送をより円滑に行うことができるので、より安全かつ効率的に物質を取扱いすることが可能となる。
また、不活性ガスの導入機構において、フランジ、ねじ込み等の配管継手で採用される連結形式により、連結部から移送用予備室に供給するための配管と移送用予備室とが接続されてもよいし、図1に示されるように移送用予備室に直接接続されていてもよい。
When the preliminary transfer chamber is cylindrical, as shown in Fig. 1, the inert gas introduction mechanism is preferably provided on the side surface thereof. More specifically, the piping for supplying the inert gas from the connecting portion to the preliminary transfer chamber is preferably connected to the side surface of the preliminary transfer chamber. This connection allows for more stable introduction of the inert gas, thereby ensuring safety and enabling smoother transfer of substances, among other things, and enabling safer and more efficient handling of substances.
In the inert gas introduction mechanism, the piping for supplying the inert gas from the connecting part to the transfer preparation chamber may be connected to the transfer preparation chamber by a connection method such as a pipe joint with a flange or a screw, or may be directly connected to the transfer preparation chamber as shown in FIG. 1.
不活性ガスの排出機構は、不活性ガスを移送用予備室から排出できればよく、その他特に制限はなく、例えば図1に示されるように、移送用予備室から不活性ガスの排気ラインに排出する連結部、当該連結部までの配管及び当該配管内の仕切り弁を備えていることが好ましい。仕切り弁を備えることで、後述する移送方法をより容易に行うことが可能となり、利便性が向上する。 The inert gas exhaust mechanism is not particularly limited as long as it can exhaust the inert gas from the transfer preparatory chamber. For example, as shown in Figure 1, it is preferable that it includes a connection section that exhausts the inert gas from the transfer preparatory chamber to an inert gas exhaust line, piping to the connection section, and a gate valve within the piping. The inclusion of a gate valve makes it easier to carry out the transfer method described below, improving convenience.
不活性ガスの排出機構は、図1に示されるように、移送用予備室が筒状である場合、その側面に設けられることが好ましい。より具体的には、不活性ガスを、移送用予備室から排出するための配管は、移送用予備室の側面に接続されていることが好ましい。このように接続されていることで、より安定した不活性ガスの排出が可能となるため、安全性を担保しつつ、とりわけ物質の移送をより円滑に行うことができるので、より安全かつ効率的に物質を取扱いすることが可能となる。
また、不活性ガスの導入機構において、フランジ、ねじ込み等の配管継手で採用される連結形式により、移送用予備室から排出するための配管と移送用予備室とが接続されてもよいし、図1に示されるように移送用予備室に直接接続されていてもよい。
When the preliminary transfer chamber is cylindrical, as shown in Fig. 1, the inert gas exhaust mechanism is preferably provided on the side of the chamber. More specifically, the piping for exhausting the inert gas from the preliminary transfer chamber is preferably connected to the side of the preliminary transfer chamber. This connection allows for more stable exhaust of the inert gas, ensuring safety and enabling smoother transfer of substances, among other things, and enabling safer and more efficient handling of substances.
In addition, in the inert gas introduction mechanism, the piping for discharging the gas from the transfer preparation chamber may be connected to the transfer preparation chamber by a connection method such as a pipe joint with a flange or a screw, or may be directly connected to the transfer preparation chamber as shown in FIG. 1.
本実施形態の物質移送装置で用いられる不活性ガスとしては、例えばヘリウム、アルゴン等の希ガス;窒素等を採用することができ、中でも汎用性の高さを考慮すると窒素が好ましい。 The inert gas used in the material transfer device of this embodiment can be, for example, a rare gas such as helium or argon; nitrogen, etc., with nitrogen being preferred in particular given its versatility.
〔物質の移送方法〕
本実施形態の物質の移送方法は、
移送用予備室と、移送物質入口部及び移送物質出口部と、不活性ガスの導入機構及び排出機構と、を備え、
前記移送物質入口部及び移送物質出口部は、前記移送用予備室に設けられ、かつ物質用第一容器の第一物質入口部及び第一物質出口部並びに物質用第二容器の第二物質移送口部と連結可能であり、
前記不活性ガスの導入機構は前記移送用予備室に不活性ガスを導入し、前記不活性ガスの排出機構は前記移送用予備室から不活性ガスを排出する、
硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質の移送装置を用い、
下記(1A)~(3A)の操作を行う、物質の移送方法、
である。
(1A)前記移送物質入口部と前記物質貯用第一容器の物質出口部に設けられた弁1aとを連結し、前記移送物質出口部と前記物質用第二容器の第二物質移送口部に設けられた弁2とを連結する。
(2A)前記弁1a及び弁2を閉とし、前記不活性ガスの導入機構及び排出機構により不活性ガスの供給及び排出を行い、不活性ガスを前記移送用予備室に充填する。
(3A)前記不活性ガスの供給及び排出を停止し、前記弁1a及び弁2を開とし、前記物質用第一容器に貯留される物質を、前記物質用第二容器に移送する。
[Method for transferring substances]
The substance transfer method of this embodiment includes:
The apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism,
the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber;
using a transfer device for a substance containing at least one atom selected from a sulfur atom and a halogen atom,
A method for transferring a substance, comprising the steps of (1A) to (3A) below:
is.
(1A) The transfer substance inlet portion is connected to a valve 1a provided at the substance outlet portion of the first substance storage container, and the transfer substance outlet portion is connected to a valve 2 provided at the second substance transfer port portion of the second substance container.
(2A) The valves 1a and 2 are closed, and the inert gas is supplied and discharged by the inert gas introduction mechanism and discharge mechanism, filling the inert gas into the transfer preliminary chamber.
(3A) The supply and discharge of the inert gas are stopped, the valves 1a and 2 are opened, and the substance stored in the first substance container is transferred to the second substance container.
既述のように、本実施形態の物質の移送方法は、上記本実施形態の物質移送装置を採用するものである。本実施形態の物質の移送方法で採用される、物質移送装置の構成は、上記本実施形態の物質移送装置について説明したとおりである。 As already mentioned, the material transfer method of this embodiment employs the material transfer device of this embodiment. The configuration of the material transfer device employed in the material transfer method of this embodiment is as described above for the material transfer device of this embodiment.
本実施形態の物質の移送方法では、本実施形態の物質移送装置を用いて、上記(1A)~(3A)の手順で操作を行う。操作(1A)~(3A)において使用する弁1a及び弁2は、図1においては物質用第一容器及び物質用第二容器が備えるものとして示されているが、物質移送装置が有する弁であってもよい。 In the material transfer method of this embodiment, the material transfer device of this embodiment is used to perform the operations in the above steps (1A) to (3A). Valve 1a and valve 2 used in operations (1A) to (3A) are shown in Figure 1 as being provided in the first material container and second material container, but they may also be valves provided in the material transfer device.
操作(1A)は、本実施形態の物質移送装置と、物質用第一容器及び物質用第二容器と連結する操作である。次いで行う操作(2A)は、物質用第一容器から物質用第二容器に物質を移送する前に、予め移送用予備室内を不活性ガスで充填する操作である。この操作により、物質が移送用予備室内を通過しても、大気中の水分等との反応が生じることがなく、より安全に物質の移送を行うことができる。 Operation (1A) is an operation for connecting the substance transfer device of this embodiment to the first substance container and the second substance container. The next operation (2A) is an operation for filling the preliminary transfer chamber with an inert gas before transferring the substance from the first substance container to the second substance container. This operation prevents the substance from reacting with moisture in the atmosphere as it passes through the preliminary transfer chamber, allowing for safer substance transfer.
操作(3A)は、物質用第二容器に貯留される物質を、物質用第一容器から物質用第二容器に移送する操作である。上記操作(1A)及び(2A)によって、移送用予備室内を不活性ガスで充填し、大気中の水分等の一切の水分を除去した環境下で、物質の移送を行うことができるので、安全性を担保しつつ、とりわけ物質の移送をより円滑に行うことができるので、より安全かつ効率的に物質を取扱いすることが可能となる。 Operation (3A) is an operation in which the substance stored in the second substance container is transferred from the first substance container to the second substance container. By performing operations (1A) and (2A) above, the transfer chamber is filled with inert gas, and the substance can be transferred in an environment where all moisture, including atmospheric moisture, has been removed. This ensures safety and, in particular, allows the substance to be transferred more smoothly, making it possible to handle the substance more safely and efficiently.
また、本実施形態の物質の移送方法は、上記操作(3A)に次いで、上記操作(2A)、下記の操作(4A)及び(5A)の操作を行うことが好ましい。
(4A)前記物質用第二容器及び弁2を前記移送物質出口部から取り外す。
(5A)前記移送物質出口部に、閉止フランジを取り付ける。
In addition, in the method for transferring a substance according to the present embodiment, it is preferable to carry out the above-mentioned operation (3A) followed by the above-mentioned operation (2A) and the following operations (4A) and (5A).
(4A) The second substance container and valve 2 are removed from the transfer substance outlet.
(5A) A closing flange is attached to the outlet portion of the transfer substance.
操作(3A)に次いで、操作(2A)の操作を行うことで、物質を移送して貯留する物質用第二容器を物質用第一容器から安全に取り外すことができる、すなわち下記操作(4A)の操作を安全に行うことができ、取り外した物質用第二容器を所望の場所に搬送することが可能となる。さらに、操作(5A)の操作を行うことで、物質用第一容器と外気との縁切りが可能となる。仮に物質用第一容器の内部に物質が残留しており、内部に残留した物質が弁1aを通過したとしても、不活性ガスが充填された物質移送装置に貯留されることとなり、かつ閉止フランジにより物質移送装置に水分を含む大気等が流入することがないため、物質と大気中の水分等との反応が生じることがなく、安全な物質の取扱いが可能となる。 By performing operation (2A) following operation (3A), the second substance container, which transfers and stores the substance, can be safely removed from the first substance container. This means that operation (4A) below can be performed safely, and the removed second substance container can be transported to the desired location. Furthermore, by performing operation (5A), it is possible to isolate the first substance container from the outside air. Even if substance remains inside the first substance container and passes through valve 1a, it will be stored in the substance transfer device filled with inert gas, and the closing flange prevents atmospheric air containing moisture from entering the substance transfer device. This prevents the substance from reacting with moisture in the atmosphere, allowing for safe handling of the substance.
本実施形態の物質の移送方法は、物質用第一容器から物質用第二容器への物質の移送を行う方法を想定している。物質用第一容器及び物質用第二容器は、例えば物質の混合、乾燥、粉砕、貯留、保管、移送等の各用途に用いられる容器であり、本実施形態の物質の移送方法では、物質用第一容器は、物質の混合、乾燥、粉砕及び貯留等の用途に用いられ、物質用第二容器は、物質用第一容器内に貯留された物質を他の場所に移送するために用いられる容器となる。より具体的には、例えば硫化物固体電解質の製造装置により製造され、物質用第一容器に貯留された硫化物固体電解質を、製品として出荷する際に、当該硫化物固体電解質を移送した物質用第二容器で出荷する、といったことが想定される。 The substance transfer method of this embodiment is intended to be a method of transferring a substance from a first substance container to a second substance container. The first substance container and the second substance container are containers used for various purposes, such as mixing, drying, grinding, storing, preserving, and transferring substances. In the substance transfer method of this embodiment, the first substance container is used for purposes such as mixing, drying, grinding, and storing substances, and the second substance container is a container used to transfer the substance stored in the first substance container to another location. More specifically, it is intended that, for example, a sulfide solid electrolyte produced by a sulfide solid electrolyte production apparatus and stored in the first substance container is shipped as a product in the second substance container into which the sulfide solid electrolyte was transferred.
物質の移送方法について、本実施形態の物質の移送方法とは別の実施形態として、物質用第二容器から物質用第一容器への物質の移送を行うことも可能である。既述のように、図1では、「第一物質入口部(出口部)」、「第一物質出口部(入口部)」と記載されており、第一物質入口部は、第一物質出口部となり得、第一物質出口部は第一物質入口部となり得る。この場合、図2に示されるように、物質用第一容器と物質用第二容器とを、本実施形態の物質移送装置を介して連結することで、物質用第二容器に貯留される物質を、物質用第一容器に移送することが可能となる。 Regarding the method for transferring a substance, as an embodiment different from the method for transferring a substance of this embodiment, it is also possible to transfer a substance from a second substance container to a first substance container. As mentioned above, Figure 1 describes a "first substance inlet (outlet)" and a "first substance outlet (inlet)," and the first substance inlet can be a first substance outlet, and the first substance outlet can be a first substance inlet. In this case, as shown in Figure 2, by connecting the first substance container and the second substance container via the substance transfer device of this embodiment, it is possible to transfer the substance stored in the second substance container to the first substance container.
本実施形態の物質の移送方法とは別の実施形態の物質の移送方法は、
移送用予備室と、移送物質入口部及び移送物質出口部と、不活性ガスの導入機構及び排出機構と、を備え、
前記移送物質入口部及び移送物質出口部は、前記移送用予備室に設けられ、かつ物質用第一容器の第一物質入口部及び第一物質出口部並びに物質用第二容器の第二物質移送口部と連結可能であり、
前記不活性ガスの導入機構は前記移送用予備室に不活性ガスを導入し、前記不活性ガスの排出機構は前記移送用予備室から不活性ガスを排出する、
硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質の移送装置を用い、
下記(1B)~(3B)の操作を行う、物質の移送方法、である。
(1B)前記移送物質入口部と前記物質用第二容器の第二物質移送口部に設けられた弁2とを連結し、前記移送物質出口部と前記物質用第一容器の第一物質入口部に設けられた弁1bとを連結する。
(2B)前記弁1b及び弁2を閉とし、前記不活性ガスの導入機構及び排出機構により不活性ガスの供給及び排出を行い、不活性ガスを前記移送用予備室に充填する。
(3B)前記不活性ガスの供給及び排出を停止し、前記弁1b及び弁2を開とし、前記物質用第二容器に貯留される物質を、前記物質用第一容器に移送する。
A method for transferring a substance according to another embodiment different from the method for transferring a substance according to this embodiment includes the following steps:
The apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism,
the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber;
using a transfer device for a substance containing at least one atom selected from a sulfur atom and a halogen atom,
A method for transferring a substance, comprising the following operations (1B) to (3B):
(1B) The transfer substance inlet portion is connected to a valve 2 provided at the second substance transfer port portion of the second substance container, and the transfer substance outlet portion is connected to a valve 1b provided at the first substance inlet portion of the first substance container.
(2B) The valves 1b and 2 are closed, and the inert gas is supplied and discharged by the inert gas introduction mechanism and discharge mechanism, filling the inert gas into the transfer preliminary chamber.
(3B) The supply and discharge of the inert gas are stopped, the valves 1b and 2 are opened, and the substance stored in the second substance container is transferred to the first substance container.
本実施形態の物質の移送方法とは別の実施形態の物質の移送方法では、物質用第一容器は、物質の混合、乾燥、粉砕及び貯留等の用途に用いられ、物質用第二容器は、物質用第一容器とは別の場所で受け入れた物体を、物質用第一容器に移送するために用いられる容器となる。より具体的には、例えば市販品又は別の製造装置で製造した固体電解質原料を物質用第二容器に移送し、固体電解質原料を貯留する物質用第二容器を物質用第一容器と物質移送装置を介して連結し、物質用第二容器から物質用第一容器に固体電解質原料を移送し、これを硫化物固体電解質の製造に用いる、といったことが想定される。ここで、市販品又は別の製造装置で製造した固体電解質原料を物質用第二容器に移送する場合は、上記本実施形態の物質の移送方法に準じて物質を物質用第二容器に移送すればよい。 In a substance transfer method according to a different embodiment from the substance transfer method of this embodiment, the first substance container is used for purposes such as mixing, drying, grinding, and storing substances, and the second substance container is a container used to transfer an object received at a location separate from the first substance container to the first substance container. More specifically, for example, a solid electrolyte raw material that is commercially available or produced by a different manufacturing device is transferred to the second substance container, the second substance container storing the solid electrolyte raw material is connected to the first substance container via a substance transfer device, and the solid electrolyte raw material is transferred from the second substance container to the first substance container and used to produce a sulfide solid electrolyte. When a solid electrolyte raw material that is commercially available or produced by a different manufacturing device is transferred to the second substance container, the substance can be transferred to the second substance container in a manner similar to the substance transfer method of this embodiment.
〔物質用容器の内部残留物の除去方法〕
本実施形態の物質用容器の内部残留物の除去方法は、
移送用予備室と、移送物質入口部及び移送物質出口部と、不活性ガスの導入機構及び排出機構と、を備え、
前記移送物質入口部及び移送物質出口部は、前記移送用予備室に設けられ、かつ物質用第一容器の第一物質入口部及び第一物質出口部並びに物質用第二容器の第二物質移送口部と連結可能であり、
前記不活性ガスの導入機構は前記移送用予備室に不活性ガスを導入し、前記不活性ガスの排出機構は前記移送用予備室から不活性ガスを排出する、
硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質の移送装置を用い、
下記(1B)及び(2B)の操作を行う、物質用容器の内部残留物の除去方法、
である。
(1B)前記移送物質入口部と前記物質用第一容器の物質出口部に設けられた弁1aとを連結する。
(2B)前記弁1aを開とし、前記不活性ガスの導入機構及び排出機構により不活性ガスの供給及び排出を行い、不活性ガスを前記移送用予備室及び前記物質用第一容器に充填する。
[Method for removing internal residue from a substance container]
The method for removing internal residues from a substance container according to this embodiment includes the steps of:
The apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism,
the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber;
using a transfer device for a substance containing at least one atom selected from a sulfur atom and a halogen atom,
A method for removing internal residues from a substance container, comprising the steps of (1B) and (2B) below:
is.
(1B) The transfer substance inlet is connected to the valve 1a provided at the substance outlet of the first substance container.
(2B) The valve 1a is opened, and the inert gas is supplied and discharged by the inert gas introduction mechanism and discharge mechanism, filling the inert gas into the transfer pre-chamber and the first substance container.
既述のように、本実施形態の物質用容器の内部残留物の除去方法は、上記本実施形態の物質移送装置を採用するものである。本実施形態の物質用容器の内部残留物の除去方法で採用される、物質移送装置の構成は、上記本実施形態の物質移送装置について説明したとおりである。 As already mentioned, the method for removing internal residue from a substance container of this embodiment employs the substance transfer device of this embodiment. The configuration of the substance transfer device employed in the method for removing internal residue from a substance container of this embodiment is as described above for the substance transfer device of this embodiment.
本実施形態の物質用容器の内部残留物の除去方法では、本実施形態の物質移送装置を用いて、上記(1B)及び(2B)の手順で操作を行う。操作(1B)及び(2B)において使用する弁1aは、図1においては物質用第一容器及び物質用第二容器が備えるものとして示されているが、物質移送装置が有する弁であってもよい。 In the method for removing internal residue from a substance container of this embodiment, the substance transfer device of this embodiment is used to perform the operations (1B) and (2B) described above. Valve 1a used in operations (1B) and (2B) is shown in Figure 1 as being provided in the first substance container and the second substance container, but it may also be a valve provided in the substance transfer device.
また、本実施形態の物質用容器の内部残留物の除去方法では、不活性ガスの導入機構により、物質用第一容器に設けられた不活性ガス導入口より不活性ガスを導入することが好ましい。これにより、より効率的に物質用容器の内部残留物を除去することが可能となる。その結果、より安全かつ効率的に物質を取扱いすることができ、製造装置の稼働率の向上を図ることもできる。 Furthermore, in the method for removing internal residues from a substance container of this embodiment, it is preferable to introduce an inert gas through an inert gas inlet provided in the first substance container using an inert gas introduction mechanism. This makes it possible to more efficiently remove internal residues from the substance container. As a result, substances can be handled more safely and efficiently, and the operating rate of the manufacturing equipment can also be improved.
本実施形態の物質移送装置、物質の移送方法及び物質用容器の内部残留物の除去方法は、硫化物固体電解質の製造装置に好適に用いられる。硫化物固体電解質の製造装置により得られた硫化物固体電解質は、高いイオン伝導度を有するものであるため、固体電解質又は電極合材として、リチウムイオン電池に、とりわけ、パソコン、ビデオカメラ、及び携帯電話等の情報関連機器や通信機器、また自動車等の車両等に用いられるリチウムイオン電池、中でも全固体電池に好適に用いられる。 The substance transfer device, substance transfer method, and method for removing internal residue from a substance container of this embodiment are suitable for use in a sulfide solid electrolyte manufacturing device. The sulfide solid electrolyte obtained by the sulfide solid electrolyte manufacturing device has high ionic conductivity, and is therefore suitable for use as a solid electrolyte or electrode composite in lithium ion batteries, particularly lithium ion batteries used in information-related devices and communication devices such as personal computers, video cameras, and mobile phones, as well as vehicles such as automobiles, and particularly all-solid-state batteries.
Claims (9)
移送用予備室と、移送物質入口部及び移送物質出口部と、不活性ガスの導入機構及び排出機構と、を備え、
前記移送物質入口部及び移送物質出口部は、前記移送用予備室に設けられ、かつ物質用第一容器の第一物質入口部及び第一物質出口部並びに物質用第二容器の第二物質移送口部と連結可能であり、
前記不活性ガスの導入機構は前記移送用予備室に不活性ガスを導入し、前記不活性ガスの排出機構は前記移送用予備室から不活性ガスを排出する、
物質移送装置。 An apparatus for transferring a substance containing at least one atom selected from a sulfur atom and a halogen atom,
The apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism,
the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber;
Material transfer equipment.
前記移送物質入口部及び移送物質出口部は、前記移送用予備室に設けられ、かつ物質用第一容器の第一物質入口部及び第一物質出口部並びに物質用第二容器の第二物質移送口部と連結可能であり、
前記不活性ガスの導入機構は前記移送用予備室に不活性ガスを導入し、前記不活性ガスの排出機構は前記移送用予備室から不活性ガスを排出する、
硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質の移送装置を用い、
下記(1A)~(3A)の操作を行う、物質の移送方法。
(1A)前記移送物質入口部と前記物質用第一容器の物質出口部に設けられた弁1aとを連結し、前記移送物質出口部と前記物質用第二容器の第二物質移送口部に設けられた弁2とを連結する。
(2A)前記弁1a及び弁2を閉とし、前記不活性ガスの導入機構及び排出機構により不活性ガスの供給及び排出を行い、不活性ガスを前記移送用予備室に充填する。
(3A)前記不活性ガスの供給及び排出を停止し、前記弁1a及び弁2を開とし、前記物質用第一容器に貯留される物質を、前記物質用第二容器に移送する。 The apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism,
the transfer substance inlet and transfer substance outlet are provided in the transfer prechamber and can be connected to the first substance inlet and first substance outlet of the first substance container and the second substance transfer port of the second substance container;
the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber;
using a transfer device for a substance containing at least one atom selected from a sulfur atom and a halogen atom,
A method for transferring a substance, comprising the following operations (1A) to (3A):
(1A) The transfer substance inlet portion is connected to a valve 1a provided at the substance outlet portion of the first substance container, and the transfer substance outlet portion is connected to a valve 2 provided at the second substance transfer port portion of the second substance container.
(2A) The valves 1a and 2 are closed, and the inert gas is supplied and discharged by the inert gas introduction mechanism and discharge mechanism, filling the inert gas into the transfer preliminary chamber.
(3A) The supply and discharge of the inert gas are stopped, the valves 1a and 2 are opened, and the substance stored in the first substance container is transferred to the second substance container.
(4A)前記物質用第二容器及び弁2を前記移送物質出口部から取り外す。
(5A)前記移送物質出口部に、閉止フランジを取り付ける。 7. The method for transferring a substance according to claim 6, wherein the steps (3A) are followed by the steps (2A) and (4A) and (5A) below.
(4A) The second substance container and valve 2 are removed from the transfer substance outlet.
(5A) A closing flange is attached to the outlet portion of the transfer substance.
前記前記移送物質入口部及び移送物質出口部は、前記移送用予備室に設けられ、かつ物質用第一容器の第一物質入口部及び第一物質出口部並びに物質用第二容器の第二物質移送口部と連結可能であり、
前記不活性ガスの導入機構は前記移送用予備室に不活性ガスを導入し、前記不活性ガスの排出機構は前記移送用予備室から不活性ガスを排出する、
硫黄原子及びハロゲン原子から選ばれる少なくとも一の原子を含む物質の移送装置を用い、
下記(1B)及び(2B)の操作を行う、物質用容器の内部残留物の除去方法。
(1B)前記移送物質入口部と前記物質用第一容器の物質出口部に設けられた弁1aとを連結する。
(2B)前記弁1aを開とし、前記不活性ガスの導入機構及び排出機構により不活性ガスの供給及び排出を行い、不活性ガスを前記移送用予備室及び前記物質用第一容器に充填する。 The apparatus comprises a transfer preliminary chamber, a transfer substance inlet and a transfer substance outlet, and an inert gas introduction mechanism and an exhaust mechanism,
the transfer substance inlet and transfer substance outlet are provided in the transfer pre-chamber and can be connected to a first substance inlet and a first substance outlet of a first substance container and a second substance transfer port of a second substance container;
the inert gas introduction mechanism introduces the inert gas into the transfer preliminary chamber, and the inert gas exhaust mechanism exhausts the inert gas from the transfer preliminary chamber;
using a transfer device for a substance containing at least one atom selected from a sulfur atom and a halogen atom,
A method for removing internal residues from a substance container, comprising the steps of (1B) and (2B) below.
(1B) The transfer substance inlet is connected to the valve 1a provided at the substance outlet of the first substance container.
(2B) The valve 1a is opened, and the inert gas is supplied and discharged by the inert gas introduction mechanism and discharge mechanism, filling the inert gas into the transfer pre-chamber and the first substance container.
9. The method for removing internal residues from a substance container according to claim 8, wherein the inert gas introducing mechanism introduces the inert gas from an inert gas inlet provided in the first substance container.
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