CN111141157A - Industrial grade glycerine processing is with glycerine steam condensation collection device - Google Patents
Industrial grade glycerine processing is with glycerine steam condensation collection device Download PDFInfo
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- CN111141157A CN111141157A CN201911245784.3A CN201911245784A CN111141157A CN 111141157 A CN111141157 A CN 111141157A CN 201911245784 A CN201911245784 A CN 201911245784A CN 111141157 A CN111141157 A CN 111141157A
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- glycerol
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- pipe
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- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 title claims abstract description 367
- 238000012545 processing Methods 0.000 title claims abstract description 23
- 235000011187 glycerol Nutrition 0.000 title claims description 135
- 238000009833 condensation Methods 0.000 title claims description 85
- 230000005494 condensation Effects 0.000 title claims description 85
- 238000005192 partition Methods 0.000 claims description 11
- 238000004821 distillation Methods 0.000 claims description 8
- 230000000149 penetrating effect Effects 0.000 claims description 7
- 230000005540 biological transmission Effects 0.000 claims description 4
- 238000004140 cleaning Methods 0.000 claims description 4
- 238000012423 maintenance Methods 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 8
- 238000001816 cooling Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000007788 liquid Substances 0.000 description 4
- 230000007547 defect Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 238000004378 air conditioning Methods 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 241000208125 Nicotiana Species 0.000 description 1
- 235000002637 Nicotiana tabacum Nutrition 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 235000003599 food sweetener Nutrition 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 238000009499 grossing Methods 0.000 description 1
- 239000003906 humectant Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- -1 papermaking Substances 0.000 description 1
- 239000000546 pharmaceutical excipient Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 239000003765 sweetening agent Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 239000002562 thickening agent Substances 0.000 description 1
- UFTFJSFQGQCHQW-UHFFFAOYSA-N triformin Chemical compound O=COCC(OC=O)COC=O UFTFJSFQGQCHQW-UHFFFAOYSA-N 0.000 description 1
- 239000003039 volatile agent Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 229910001868 water Inorganic materials 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B1/00—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
- F28B1/06—Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using air or other gas as the cooling medium
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B9/00—Auxiliary systems, arrangements, or devices
- F28B9/08—Auxiliary systems, arrangements, or devices for collecting and removing condensate
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention relates to the technical field of glycerol processing equipment, and provides a glycerol steam condensing and collecting device for industrial glycerol processing, aiming at solving the problem that the existing industrial glycerol steam condensing and collecting device is in a one-way passing condensing mode, on one hand, the condensing device cannot keep steady-state operation, on the other hand, the condensing efficiency is low, the effect is poor, and glycerol still remains in the discharged glycerol steam, so that glycerol is wasted. The invention is especially suitable for condensing and collecting industrial-grade glycerol, and has higher social use value and application prospect.
Description
Technical Field
The invention relates to the technical field of glycerol processing equipment, in particular to a glycerol steam condensing and collecting device for industrial-grade glycerol processing.
Background
Glycerol, also known as glycerol, is colorless, odorless, sweet in flavor, clear, viscous and liquid in appearance, and is an organic substance.
Glycerol is a chemical with wide application, is widely applied to the industrial fields of coating, papermaking, textile, food, medicine, tobacco, cosmetics and the like, is mainly used as an excipient, a humectant, a smoothing agent, a sweetening agent, a thickening agent, an antifreezing agent, an emulsifying agent and the like, and can be divided into medicinal grade and industrial grade according to the purity of the glycerol. The traditional sources of the industrial-grade glycerol are mainly grease hydrolysis byproducts, byproducts of starch fermentation and diesel oil production, and the crude product glycerol prepared by synthesis is purified by the working procedures of filtering, concentrating, dehydrating, chemical additives, distilling and the like to obtain the industrial-grade glycerol.
Crude glycerol contains a large amount of impurities such as water, sodium chloride, sodium sulfate and organic volatiles, and further refining of the crude glycerol is required to meet the requirements of industrial applications. The glycerol refining production generally adopts the working procedures of evaporation, distillation, deodorization, decoloration and the like to produce products meeting the national standard; wherein the glycerol vapor after distillation is condensed and collected to become an important part of the product.
The existing industrial glycerin steam condensing and collecting device is often a one-way passing condensing mode when glycerin steam is condensed, on one hand, the condensing device cannot keep steady-state operation, after tube pass fluid exchanges heat with a condenser again, the temperature of the glycerin steam is higher, the design temperature cannot be reached, on the other hand, the condensing efficiency is lower, the condensing effect is poor, glycerin can still be remained in the discharged glycerin steam, and the glycerin steam is wasted.
The patent with publication number CN205049032U discloses a high-efficiency condensing device for triglyceride process, which comprises a condenser, wherein the condenser consists of a condenser plate component and a frame, the condenser plate component consists of condenser plates A and condenser plates B which are arranged alternately and is provided with a partition plate, a reticular protective cover is arranged outside the condenser plate component and is fixed by the frame, and an air cooling device is arranged on a guide pipe connected with the condenser, so that the heat exchange effect of the condenser is enhanced, but the device has the defect that the ideal condensing effect cannot be achieved. Therefore, a glycerol steam condensing and collecting device for industrial-grade glycerol processing is provided.
Disclosure of Invention
Technical problem to be solved
Aiming at the defects of the prior art, the invention provides a glycerol steam condensing and collecting device for industrial glycerol processing, which overcomes the defects of the prior art, has reasonable design and compact structure, and aims to solve the problems that the existing industrial glycerol steam condensing and collecting device is in a one-way passing condensing mode, on one hand, a condensing device cannot keep steady-state operation, on the other hand, the condensing efficiency is low, the condensing effect is poor, and glycerol still remains in the discharged glycerol steam, so that the glycerol is wasted.
(II) technical scheme
In order to achieve the purpose, the invention is realized by the following technical scheme:
a glycerol steam condensation and collection device for industrial-grade glycerol processing comprises a condensation cabinet and a base which is arranged at the lower end of the condensation cabinet and used for supporting, wherein two shunt tubes are inserted into the top wall of the condensation cabinet in a penetrating manner, the other ends of the shunt tubes are connected with the same gas pipe in a penetrating manner, the other end of the gas pipe is communicated with a gas transmission port of a distillation tower, a bottom plate is transversely arranged at the lower part of an inner cavity of the condensation cabinet and divides the condensation cabinet into a condensation cavity and an equipment cavity from top to bottom, two vertical partition plates are fixedly arranged in the inner cavity of the condensation cavity and divide the condensation cavity into a glycerol collection cavity at two sides and an exhaust cavity at the middle part, a plurality of transverse partition plates are arranged in the inner cavity of the glycerol collection cavity at equal intervals, and the glycerol collection cavity is divided into a plurality;
the condensing boxes are arranged in the inner cavities of the collecting sub-chambers and are in through connection through communicating pipes, the condensing box positioned at the top is in through connection with the flow dividing pipe, the two condensing boxes at the bottom are in through connection with the same exhaust pipe II, the other end of the exhaust pipe II extends to the outer cavity of the condensing cabinet, a glycerin output branch pipe is arranged at the lower part of the rear wall of the condensing box in through connection, the other ends of the glycerin output branch pipes reach the outer cavity of the condensing cabinet and are connected to the same oil conveying main pipe, a valve III is arranged on the glycerin output branch pipe, the output end of the oil conveying main pipe is in through connection with the top wall of a glycerin tank, and the glycerin tank is;
install the air-cooler in the inner chamber in equipment cavity, and install the cold air duct on the air-cooler output, the cold air duct extends into the inner chamber in exhaust chamber and through connection has a plurality of intake pipes, and the intake pipe respectively with every collect the locellus through connection.
Furthermore, be equipped with the S-shaped return passage that is used for glycerine gas to pass through in the inner chamber of condensation box, the perforated plate is installed to the inner chamber lower part level of condensation box, and is formed with the glycerine passageway between the inner chamber lower part of perforated plate and condensation box.
Furthermore, the input end of the glycerol output branch pipe is communicated with the glycerol channel.
Furthermore, all install the branch pipe of giving vent to anger with exhaust chamber through connection on the lateral wall of collecting the locellus, and install valve II on the branch pipe of giving vent to anger, the back wall upper portion of exhaust chamber is link up and is installed and extend to the blast pipe I of condensation cabinet exocoel.
Furthermore, a concave placing chamber for placing the glycerol tank is formed at the lower part of the rear wall of the condensation cabinet, and supporting plates are fixedly connected to the two side edges of the concave structure.
Furthermore, a valve I is arranged on the gas conveying pipe.
Furthermore, a cabinet door for cleaning and maintenance is installed on the front wall of the condensation cabinet corresponding to the position of the condensation cavity.
Furthermore, a control panel is installed on the lower portion of the front end of the condensation cabinet, a display screen and a control button are arranged on the control panel, and a PLC is arranged in the control panel.
(III) advantageous effects
The embodiment of the invention provides a glycerol steam condensing and collecting device for industrial-grade glycerol processing, which has the following beneficial effects:
1. through the integrated configuration of bottom plate, two perpendicular division boards and a plurality of cross slab, divide a plurality of collections locuses by bottom plate, two perpendicular division boards and a plurality of cross slabs to and the high-efficient condensation that carries out glycerine at the condensation box that collects the locuses setting, the cold air lets in a plurality of collections locuses in the cooling process and carries out the condensation to glycerine steam fast, and the condensation effect is better.
2. Through the integrated configuration of air-cooler, cold air duct and condensation box, the air-cooler starts, inputs air conditioning in the cavity to each collection locellus respectively for the cooling of glycerine steam, air conditioning can dwell time be more of a specified duration, makes the glycerine steam of process in the condensation box continuously exothermic, the effectual condensation cost that has reduced.
3. Through communicating pipe realize the through connection between a plurality of condensation boxes, guarantee that glycerine steam carries out condensation in proper order in a plurality of condensation boxes, come out the glycerine condensation that carries in the glycerine steam, form the glycerine liquid drop through glycerine output branch pipe and oil transportation house steward input glycerine case, accomplish the condensation and collect, the effectual traditional glycerine steam single condensation of having avoided, problem that the condensation effect through equipment is poor.
Drawings
The above features, technical features, advantages and implementations of a glycerol vapor condensation collection device for industrial-grade glycerol processing will be further described in the following detailed description of preferred embodiments in a clearly understandable manner with reference to the accompanying drawings.
FIG. 1 is a schematic view of the appearance of a condensing and collecting apparatus for industrial-grade glycerin vapor used in the process of the present invention;
FIG. 2 is a schematic structural diagram of a condensing and collecting device for industrial glycerol vapor in glycerol processing according to the present invention;
FIG. 3 is a side view of a glycerol vapor condensing and collecting apparatus for industrial-grade glycerol processing according to the present invention;
FIG. 4 is a rear view of a condensing and collecting apparatus for industrial-grade glycerol vapor for glycerol processing according to the present invention;
FIG. 5 is an enlarged view of the structure A in FIG. 2 according to the present invention.
In the figure: distillation column 1, gas-supply pipe 2, shunt tubes 3, condensation cabinet 4, base 5, control panel 6, cabinet door 7, blast pipe I8, valve I9, blast pipe II 10, air-cooler 11, cold air duct 12, bottom plate 13, vertical separation board 14, cross slab 15, intake pipe 16, condensation box 17, air outlet branch pipe 18, valve II 19, communicating pipe 20, S-shaped return ring passageway 21, perforated plate 22, glycerine passageway 23, glycerine output branch pipe 24, oil transportation house steward 25, valve III 26, glycerine case 27, backup pad 28.
Detailed Description
The invention will be further illustrated with reference to the following figures 1 to 5 and examples:
example 1
A glycerol steam condensing and collecting device for industrial glycerol processing comprises a condensing cabinet 4 and a base 5 which is arranged at the lower end of the condensing cabinet 4 and used for supporting, wherein two shunt tubes 3 are inserted on the top wall of the condensing cabinet 4, the other end of the shunt tube 3 is connected with the same gas pipe 2 in a run-through way, the other end of the gas pipe 2 is communicated with a gas transmission port of the distillation tower 1, a bottom plate 13 is transversely arranged at the lower part of the inner cavity of the condensation cabinet 4, and the bottom plate 13 divides the condensation cabinet 4 into a condensation cavity and an equipment cavity from top to bottom, two vertical partition plates 14 are fixedly arranged in the inner cavity of the condensation cavity, the vertical partition plate 14 divides the condensation cavity into a glycerin collection cavity at two sides and an exhaust cavity at the middle part, a plurality of transverse partition plates 15 are equidistantly arranged in the inner cavity of the glycerin collection cavity, and the glycerin collection cavity is divided into a plurality of vertically distributed collection sub-chambers by the plurality of transverse partition plates 15;
in this embodiment, as shown in fig. 2 to 5, a condensation box 17 is installed in an inner cavity of the collection chamber, and the multiple condensation boxes 17 are connected through a communication pipe 20, the condensation box 17 located at the top is connected through a shunt tube 3, the two condensation boxes 17 located at the bottom are connected through a same exhaust pipe ii 10, the other end of the exhaust pipe ii 10 extends to an outer cavity of the condensation cabinet 4, a glycerin output branch pipe 24 is installed at the lower part of the rear wall of the condensation box 17 through a communication pipe, the other ends of the multiple glycerin output branch pipes 24 reach the outer cavity of the condensation cabinet 4 and are connected to a same oil transportation main pipe 25, a valve iii 26 is arranged on the glycerin output branch pipe 24, the output end of the oil transportation main pipe 25 is connected through the top wall of a glycerin tank 27, and the glycerin tank 27 is;
in this embodiment, as shown in fig. 2 and 5, an air cooler 11 is installed in an inner cavity of the equipment cavity, an air cooling pipe 12 is installed at an output end of the air cooler 11, the air cooling pipe 12 extends into the inner cavity of the exhaust cavity and is connected with a plurality of air inlet pipes 16 in a penetrating manner, and the air inlet pipes 16 are respectively connected with each collecting sub-chamber in a penetrating manner.
In the embodiment, glycerin vapor generated by distillation in the distillation tower 1 is injected into the inner cavity of the condensation cabinet 4 through the gas transmission pipe 2-the shunt pipe 3, and glycerin is condensed by combining the collection sub-chamber which is divided by the bottom plate 13, the two vertical partition plates 14 and the plurality of transverse partition plates 15 and the condensation box 17 which is arranged in the collection sub-chamber; the air cooler 11 is started, and cold air is respectively input into the chambers of the collecting sub-chambers and used for cooling glycerol steam; combine communicating pipe 20 to realize the through connection between a plurality of condensation boxes 17, guarantee that glycerine steam carries out condensation in proper order in a plurality of condensation boxes 17, come out the glycerine condensation that carries in the glycerine steam, form the glycerine liquid drop through glycerine output branch pipe 24 and oil transportation house steward 25 input glycerine case 27 in, accomplish the condensation and collect, the steam of the glycerine of finishing the condensation passes through II 10 discharges on the blast pipe, accomplishes the continuous condensation of glycerine and collects.
In this embodiment, as shown in fig. 5, an S-shaped loop channel 21 for glycerol gas to pass through is arranged in an inner cavity of the condensation box 17, a porous plate 22 is horizontally arranged at the lower part of the inner cavity of the condensation box 17, and a glycerol channel 23 is formed between the porous plate 22 and the lower part of the inner cavity of the condensation box 17, the S-shaped loop channel 21 can effectively prolong the stay time of glycerol vapor in the condensation box 17, so as to realize efficient condensation, and the collection and collection of glycerol droplets can be completed by combining the arrangement of the glycerol channel 23, so that the collection of glycerol is facilitated.
In this embodiment, as shown in fig. 4 and 5, the input end of the glycerin output branch pipe 24 is connected to the glycerin passage 23 in a penetrating manner, so as to ensure the output and collection of glycerin liquid.
In this embodiment, as shown in fig. 2 and 5, the side walls of the collecting sub-chambers are all provided with air outlet branch pipes 18 communicated with the air outlet chamber, the air outlet branch pipes 18 are provided with valves ii 19, the upper part of the rear wall of the air outlet chamber is provided with an air outlet pipe i 8 communicated with the outer chamber of the condensation cabinet 4, and when cold air is input, the air outlet branch pipes are used for discharging the air cooled in the collecting sub-chambers, and meanwhile, it can be understood that when the air in the collecting sub-chambers is kept at a certain temperature, the valves ii 19 can be intermittently opened to replace the cold air, so that the purpose of saving resources is achieved.
In this embodiment, as shown in fig. 1, a valve i 9 is installed on the gas pipe 2 for controlling the output of glycerol vapor.
In this embodiment, as shown in fig. 1, a cabinet door 7 for cleaning and maintenance is installed on the front wall of the condensation cabinet 4 corresponding to the position of the condensation chamber, so as to ensure the cleaning of the inside of the condensation cabinet 4 and the safe operation of each mechanism.
In this embodiment, the valve i 9, the valve ii 19, and the valve iii 26 are all electromagnetic valves, the electromagnetic valves are industrial devices controlled by electromagnetism, are automatic basic elements for controlling fluid, belong to actuators, are not limited to hydraulic pressure and pneumatic pressure, and can be matched with different circuits to realize expected control, and the accuracy and flexibility of control can be ensured.
In this embodiment, as shown in fig. 1, a control panel 6 is installed on the lower portion of the front end of the condensation cabinet 4, a display screen and a control button are arranged on the control panel 6, a PLC controller is arranged in the control panel 6, in this embodiment, the model of the PLC controller is siemens S7-300, and the control panel 6 is electrically connected with the air cooler 11, the valve i 9, the valve ii 19 and the valve iii 26.
Example 2
The difference between this embodiment and embodiment 1 is that, as shown in fig. 3 and 4, a placing chamber for placing the glycerol tank 27 is formed at the lower portion of the rear wall of the condensation cabinet 4, and supporting plates 28 are fixedly connected to the two side edges of the concave structure, so as to facilitate the glycerol tank 27 to be received, on one hand, the floor space is saved, and on the other hand, the connection with the oil transportation main pipe 25 is facilitated, so as to ensure the glycerol collection.
Other undescribed structures refer to example 1.
The embodiments of the present invention are disclosed as the preferred embodiments, but not limited thereto, and those skilled in the art can easily understand the spirit of the present invention and make various extensions and changes without departing from the spirit of the present invention.
Claims (8)
1. The glycerol steam condensation and collection device for industrial-grade glycerol processing comprises a condensation cabinet and a base which is arranged at the lower end of the condensation cabinet and used for supporting, and is characterized in that two shunt tubes are inserted into the top wall of the condensation cabinet in a penetrating manner, the other ends of the shunt tubes are connected with the same gas pipe in a penetrating manner, the other end of the gas pipe is communicated with a gas transmission port of a distillation tower, a bottom plate is transversely arranged at the lower part of an inner cavity of the condensation cabinet and divides the condensation cabinet into a condensation cavity and an equipment cavity from top to bottom, two vertical partition plates are fixedly arranged in the inner cavity of the condensation cavity and divide the condensation cavity into a glycerol collection cavity at two sides and an exhaust cavity in the middle, a plurality of transverse partition plates are equidistantly arranged in the inner cavity of the glycerol collection cavity and divide the glycerol collection cavity into a plurality of vertically distributed collection sub;
the condensing boxes are arranged in the inner cavities of the collecting sub-chambers and are in through connection through communicating pipes, the condensing box positioned at the top is in through connection with the flow dividing pipe, the two condensing boxes at the bottom are in through connection with the same exhaust pipe II, the other end of the exhaust pipe II extends to the outer cavity of the condensing cabinet, a glycerin output branch pipe is arranged at the lower part of the rear wall of the condensing box in through connection, the other ends of the glycerin output branch pipes reach the outer cavity of the condensing cabinet and are connected to the same oil conveying main pipe, a valve III is arranged on the glycerin output branch pipe, the output end of the oil conveying main pipe is in through connection with the top wall of a glycerin tank, and the glycerin tank is;
install the air-cooler in the inner chamber in equipment cavity, and install the cold air duct on the air-cooler output, the cold air duct extends into the inner chamber in exhaust chamber and through connection has a plurality of intake pipes, and the intake pipe respectively with every collect the locellus through connection.
2. The glycerol vapor condensing and collecting device for industrial-grade glycerol processing as claimed in claim 1, wherein: be equipped with the S-shaped return passage that is used for glycerine gas to pass through in the inner chamber of condensation box, the perforated plate is installed to the inner chamber lower part level of condensation box, and is formed with the glycerine passageway between the inner chamber lower part of perforated plate and condensation box.
3. The glycerol vapor condensing and collecting device for industrial-grade glycerol processing as claimed in claim 2, wherein: the input end of the glycerin output branch pipe is communicated with the glycerin channel.
4. The glycerol vapor condensing and collecting device for industrial-grade glycerol processing as claimed in claim 1, wherein: all install the branch pipe of giving vent to anger with exhaust chamber through connection on the lateral wall of collection locellus, and the branch pipe of giving vent to anger is last to install valve II, and the rear wall upper portion of exhaust chamber is link up and is installed the blast pipe I that extends to the condensation cabinet exocoel.
5. The glycerol vapor condensing and collecting device for industrial-grade glycerol processing as claimed in claim 1, wherein: the lower part of the rear wall of the condensation cabinet is provided with an inward concave placing chamber for placing the glycerol tank, and the edges of two sides of the inward concave structure are fixedly connected with supporting plates.
6. The glycerol vapor condensing and collecting device for industrial-grade glycerol processing as claimed in claim 1, wherein: and a valve I is arranged on the gas conveying pipe.
7. The glycerol vapor condensing and collecting device for industrial-grade glycerol processing as claimed in claim 1, wherein: and a cabinet door for cleaning and maintenance is arranged on the front wall of the condensation cabinet corresponding to the position of the condensation cavity.
8. The glycerol vapor condensing and collecting device for industrial-grade glycerol processing as claimed in claim 1, wherein: control panel is installed to the front end lower part of condensation cabinet, and is equipped with display screen and control button on the control panel, and control panel embeds there is the PLC controller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911245784.3A CN111141157A (en) | 2019-12-07 | 2019-12-07 | Industrial grade glycerine processing is with glycerine steam condensation collection device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911245784.3A CN111141157A (en) | 2019-12-07 | 2019-12-07 | Industrial grade glycerine processing is with glycerine steam condensation collection device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN111141157A true CN111141157A (en) | 2020-05-12 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201911245784.3A Pending CN111141157A (en) | 2019-12-07 | 2019-12-07 | Industrial grade glycerine processing is with glycerine steam condensation collection device |
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| Country | Link |
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| CN (1) | CN111141157A (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB486311A (en) * | 1935-12-23 | 1938-06-01 | Colgate Palmolive Peet Co | Improvements in distillation of glycerin and in the distillation and purification ofother volatile substances |
| CN202119296U (en) * | 2011-06-09 | 2012-01-18 | 常州市华人化工有限公司 | Combined condensation device |
| CN103965019A (en) * | 2014-04-04 | 2014-08-06 | 天长市康宁塑胶科技有限公司 | Purification production process of glycerol |
| CN205049032U (en) * | 2015-09-11 | 2016-02-24 | 弥勒市康和甘油酯有限公司 | High -efficient condensing equipment is used to triglycerides technology |
| CN208313099U (en) * | 2018-04-26 | 2019-01-01 | 清远市福泰甘油精制有限公司 | A kind of afterheat utilizing system during glycerol production |
-
2019
- 2019-12-07 CN CN201911245784.3A patent/CN111141157A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB486311A (en) * | 1935-12-23 | 1938-06-01 | Colgate Palmolive Peet Co | Improvements in distillation of glycerin and in the distillation and purification ofother volatile substances |
| CN202119296U (en) * | 2011-06-09 | 2012-01-18 | 常州市华人化工有限公司 | Combined condensation device |
| CN103965019A (en) * | 2014-04-04 | 2014-08-06 | 天长市康宁塑胶科技有限公司 | Purification production process of glycerol |
| CN205049032U (en) * | 2015-09-11 | 2016-02-24 | 弥勒市康和甘油酯有限公司 | High -efficient condensing equipment is used to triglycerides technology |
| CN208313099U (en) * | 2018-04-26 | 2019-01-01 | 清远市福泰甘油精制有限公司 | A kind of afterheat utilizing system during glycerol production |
Non-Patent Citations (1)
| Title |
|---|
| 张祉祐等: "《低温技术原理与装置 上册》", 30 June 1987, 机械工业出版社 * |
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Application publication date: 20200512 |
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| RJ01 | Rejection of invention patent application after publication |