WO1986001819A1 - Method of and apparatus for discharging pulverulent and granular substance from hermetic vertical cooling furnace - Google Patents
Method of and apparatus for discharging pulverulent and granular substance from hermetic vertical cooling furnace Download PDFInfo
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- WO1986001819A1 WO1986001819A1 PCT/JP1984/000448 JP8400448W WO8601819A1 WO 1986001819 A1 WO1986001819 A1 WO 1986001819A1 JP 8400448 W JP8400448 W JP 8400448W WO 8601819 A1 WO8601819 A1 WO 8601819A1
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- atmosphere
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- powder
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- cooling furnace
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B33/00—Discharging devices; Coke guides
- C10B33/12—Discharge valves
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D3/00—Charging; Discharging; Manipulation of charge
- F27D3/0033—Charging; Discharging; Manipulation of charge charging of particulate material
Definitions
- the present invention relates to a method and an apparatus for discharging powders in a vertical cooling furnace for powders requiring airtightness in an atmosphere in which air is shut off.
- Japanese Patent Laid-Open No. 57-36884 proposes a method for continuous cutting from a vertical cooling furnace.
- the method is not
- the spilling means is still due to the use of a seal popper with a double seal valve, which does not increase the height of the discharge device.
- FIG. 1 a method is known in which a rotary valve 1 is directly exposed to a powder outlet 5 of a vertical cooling furnace 2, but a rotor 3 is used.
- Undesired penetration of coke between the shaft and casing 4 causes increased crushing and load, and significant wear on rotor 3 and casing 4 Practical use is difficult because of the drawbacks that the airtight function cannot be guaranteed after a short operation.
- the present invention solves the above-mentioned problems and, while maintaining airtightness, a method capable of continuously discharging powders and granules, and further reducing the height of the entire equipment, and an inexpensive discharge device. For the purpose of providing.
- the powder and granules are continuously and quantitatively taken out from the lower part of the cooling chamber of the vertical cooling furnace in an atmosphere in which the air is shut off, and the air is cut off in an atmosphere where the air is cut off.
- the powder and granules taken out to the one storage unit of the rotary valve, which is provided in an airtight manner so that it is opened to the outside, are stored in a range that does not become full, and the rotor is further opened. It is characterized in that the powder in the storage section is discharged to the atmosphere by rotating the table.
- a QMK that requires airtightness
- an airtight chamber communicating with this outlet and having an opening for discharging the granular material is provided below the outlet of the granular material in the cooling chamber.
- a transfer device that continuously and quantitatively sends the granules from the granule outlet to the opening of the hermetic chamber from the outlet is installed, and at least one storage section is provided around the A rotary valve having a rotatable rotor is provided so that the storage section communicates with the opening of the airtight chamber in an airtight manner with rotation, and the drive device rotates the rotary port.
- Fig. 1 shows a vertical valve at the bottom of a vertical cooling furnace for granular materials.
- Fig. 2 is a cross-sectional view of an essential part of an example of a conventional discharge device in which a vibration feeder is installed at the bottom of a vertical cooling furnace for granular material.
- Main part sectional view showing an embodiment of the present invention provided with a rotary valve,
- FIG. 3 is a perspective view of a rotor of a rotary valve used in the present invention.
- FIG. 4 shows a 7 ° port feeder at the bottom of the vertical cooling furnace for powder and granules.
- FIG. 5 is a sectional view of a main part showing another embodiment of the present invention in which a rotary valve is provided at the discharge part of the feeder.
- FIG. Fig. 7 is a cross-sectional view of a principal part showing still another embodiment of the present invention in which a feeder is provided and a rotary valve is provided at an outlet of the roll feeder. Disclosure of the best mode for carrying out the invention
- Fig. 2 shows an airtight chamber 16 provided below the outlet 15 of the vertical cooling furnace 12 and a vibration feeder 17 as a transfer device installed in the airtight chamber. Further, in this example, a rotor valve 11 is provided adjacent to the discharge section of the vibration feeder 17.
- 13 is a rotatable port
- 14 is a casing for accommodating the rotor 13
- 18 is a rotor blade and casing.
- the inner periphery of 1'4 is slidably contacted with the inner periphery of 1'4, so that the hermeticity of the hermetic chamber 16 is maintained.
- the airtightness is maintained by direct contact between the casing and the rotor blades.
- the airtightness may be maintained by interposing a sealing means.
- the rotor 13 is preferably provided with a side plate 19 to improve airtightness, and is continuously provided by a vibrating feeder 17.
- the granular material cut out quantitatively is supplied to a supply port 20 to a rotor valve 11 and is surrounded by a rotor blade 18 and a side plate 19 around a rotor 13. It is housed in a plurality of storage portions formed radially at the same time, and is further discharged from the mouth-tally valve 11 with the rotation of the rotor 13 by a driving device (not shown). Delivery Belt Conveyor — transported by 21.
- the vibratory feeder 17 has a good quantitative cut-out property except for a large particle size (200 baskets or more), so that the rotor 18 and the side plate 19 In order not to supply more than the capacity of each space, that is, the storage unit, it is possible to control the amount of supply so as not to be full, and to add granular materials. is there. In addition, since the vibration feeder 17 is provided upstream of the rotary valve 11, the opening width a of the supply port 20 to the rotary valve 11 is limited. On the other hand, it is possible to make the falling flow width b of the granular material small, and it is possible to prevent the infiltration of the granular material between one rotor blade 18 and the casing 14. .
- the tip of the rotor blade 18 is exposed to the falling flow of the granular material at the supply port 20, but the vibration feeder 17 causes the rotor blade 18 to wear. Since the falling speed of the granular material supplied to the supply port 20 to the tally valve 11 can be minimized, it can be supplied gently and the rotor blade 18 can be prevented from wearing at the tip. In addition, the wear of this part is local, and even if a high friction material such as high cr steel is used, there is no problem in the overall equipment cost of the port-tally valve 1.1.
- a super abrasion-resistant material such as nitrogen nitride ceramic may be used for this part, or a replacement structure may be used. High airtightness can be maintained by replacing the airtightly.
- the vibration feeder 17 is inexpensive, has sufficient durability, and is highly practical.
- the compactness of the quantitative cutout device is important for the present invention, and the equipment cost can be reduced because not only the discharge device but also the entire cooling furnace can be lowered.
- the transfer device of the present invention is not limited to the vibration feeder, and as another embodiment of the present invention, the epoxy feeder is provided with a rotary valve.
- Fig. 4 shows an example of using it as a quantitative extraction device upstream of the system.
- the characteristic of the feeder 1-17 is that quantitative extraction is excellent even for the extraction of large-grained powder, and quantitative extraction is easy.
- a small sieve is used to narrow the flow width b of the supplied granular material. It is preferable to provide a cutout 11 1 to prevent the particulates from getting caught in the rotary valve 11.
- reference numeral 217 denotes a roll feeder installed in the hermetic chamber 216, and the same reference numerals as those in FIGS. 2 and 4 denote the same. The same components as those used in the illustrated embodiment are shown.
- the characteristics of the Roll Feeder II 17 are that it is simple in structure, durable, and inexpensive. In addition, the same as in the case of the combination of the 7 ° low feeder and the rotary valve, preventing the powder and particulate matter from being caught in the rotary valve 11. For this reason, it is better to provide a small shot 211 at the discharge section of the roll feeder 2 17.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)
Abstract
Description
明 細 書 気密の竪型冷却炉 ょ り 粉粒体 Description Air-tight vertical cooling furnace
を排出する方法およ び装置 技術分野お よ び背景技術 And equipment for discharging wastewater Technical field and background art
本発明は気密を要する粉粒体用の竪型冷却炉 ょ り 大 気を遮断 した雰囲気下で粉粒体を排出する方法お よ び その装置に関する。 The present invention relates to a method and an apparatus for discharging powders in a vertical cooling furnace for powders requiring airtightness in an atmosphere in which air is shut off.
気密を要する粉粒体用竪 k冷却炉の排出装置と し て は、 例えば、 コ ー ク ス炉よ り 排.出される赤熱コ ー ク ス の顕熱を回収 レ'て省エ ネ ルギ ーを計る ための コ ー ク ス 乾式消火設備の竪型冷却炉から 冷却 さ.れた コ ー ク ス を 排出する排出装置があ る。 こ れら の設備においては、 装置高 さ を低減する こ とが設傭 コ ス 卜 ダ ウ ン上重要で あ るが、 従来、 ソ連ギ: 7° ロ コ 一 ク ス の例の如 く 、 竪型 式冷却炉の底部よ り カ ツ ト ゲー ドを介 し て コ 一 ク ス を パッ チ式で切出 し、 2 重の シ ー ル弁を持つ シ ー ルホ ッ ーで気密 し、 一且コ 一 ク ヮ. 一 フ に卸 した後ヮ ー フゲ ー ト にて、 払 出ペル ト コ ン ベ ヤ ー に連続排出を行なつ てい るため、 排出装置全体の高さが大き く な る こ とは 避けら れなかった。 Is a discharge device for the granular-body vertical k cooled reactor requiring airtightness, for example, co-chromatography click scan furnace by Ri discharge. Glow co over click scan sensible heat of Te recovery Les' Ministry of e issued Ne conservation over There is a discharge device that discharges the cooled coke from the vertical cooling furnace of the dry fire extinguishing system. In these facilities, it is important to reduce the height of the equipment in terms of installation costs, but in the past, as in the case of the Soviet Union: 7 ° A patch is cut out from the bottom of the vertical cooling furnace via a cut gate by a patch type, and hermetically sealed with a seal hood with a double seal valve. And after the product has been wholesaled to one piece, the continuous discharge to the dispensing pelt conveyor is carried out at the roof gate, so the height of the entire discharge device becomes large. Was inevitable.
又、 特開昭 5 7 - 3 6 8 4 号 ( 対応米国 出願の特 許番号 4, 3 4 4 , 8 2 3 ) では、 竪型式冷却炉 ょ り 連続 切出 し を行な う 方式が提案されてい るが、 該方式 も気 密手段はやは り、 2重の シ ー ル弁を持つ シ ー ルポ ッパ 一に よつているため排出装置の高さが高 く なる こ と に は変 り ない。 Also, Japanese Patent Laid-Open No. 57-36884 (corresponding to U.S. patent application Ser. No. 4,344,823) proposes a method for continuous cutting from a vertical cooling furnace. However, the method is not The spilling means is still due to the use of a seal popper with a double seal valve, which does not increase the height of the discharge device.
さ らに、 第 1 図に示す如 く、 竪型式冷却炉 2 の粉粒 体出口 5 に直接ロ ータ リ ー弁 1 を臨ませて用いる方式 が知られているが、 ロ ータ ー 3 と ケ一 シ ング 4 との間 へのコ ークス の不所望なかみ込みによ る破砕および負 荷の増大、 ならびに ロ ータ ー 3 , ケ一 シ ソ グ 4 に著し い摩耗が生じ、 気密機能が短時間の運転で保障されな く なる等の欠点があるため、 実用 は困難である。 Further, as shown in FIG. 1, a method is known in which a rotary valve 1 is directly exposed to a powder outlet 5 of a vertical cooling furnace 2, but a rotor 3 is used. Undesired penetration of coke between the shaft and casing 4 causes increased crushing and load, and significant wear on rotor 3 and casing 4 Practical use is difficult because of the drawbacks that the airtight function cannot be guaranteed after a short operation.
. 発明の開'示 · .· DISCLOSURE OF THE INVENTION
本発明は前述の問題点を解決し、 気密を保ちなが.ら 粉粒体を連続的に排出でき、 しか も設備全体の高さを 低くする こ とができ る方法並びに安価な排出装置の提 供を 目的とする。 The present invention solves the above-mentioned problems and, while maintaining airtightness, a method capable of continuously discharging powders and granules, and further reducing the height of the entire equipment, and an inexpensive discharge device. For the purpose of providing.
こ の 目的のため、 本発明では竪型冷却炉の冷却室下 部から大気を遮断した雰囲気下で粉粒体を連続的かつ 定量的に取 り 出.し、 この大気を遞断した雰囲気中に開 口する よ う 気密状に設けられたロ ー タ リ 一弁の ロ ー '一の収納部へ取 り 出された粉粒体を満杯にならない範 囲で収容し、 さら に ロ ー タ ーを回転する こ と に よ り 収 納部の粉粒体を大気雰囲気下に排出する こ とを特徴と する。 For this purpose, according to the present invention, the powder and granules are continuously and quantitatively taken out from the lower part of the cooling chamber of the vertical cooling furnace in an atmosphere in which the air is shut off, and the air is cut off in an atmosphere where the air is cut off. The powder and granules taken out to the one storage unit of the rotary valve, which is provided in an airtight manner so that it is opened to the outside, are stored in a range that does not become full, and the rotor is further opened. It is characterized in that the powder in the storage section is discharged to the atmosphere by rotating the table.
さらに、 本発明の他の特徵によれば、 気密を要する QMK 粉粒体用の竪型冷却炉の排出装置において、 冷却室の 粉粒体出口の下部に この出口 と連通しかつ粉粒体を搬 出する ための開口を傭えた気密室を設け、 こ の気密室 内に粉粒体出口 よ り気密室の開口へ粉粒体を連続的か つ定量的に送 り 出す搬送装置を設置し、 また周囲に少 な く と も 1 つの収納部を備えかつ回転に伴ってこ の収納 部が気密室の開口 と気密状に連通する よ う 回転可能な ロ ー タ 一を有する ロ ー タ リ 一弁を設け、 駆動装置でこ の 口 一タ ーを回転させる こ と に よって粉粒体を連続的 に排出する排出装置が提供される。 Furthermore, according to another feature of the present invention, a QMK that requires airtightness In the discharge device of the vertical cooling furnace for granular materials, an airtight chamber communicating with this outlet and having an opening for discharging the granular material is provided below the outlet of the granular material in the cooling chamber. In the hermetic chamber, a transfer device that continuously and quantitatively sends the granules from the granule outlet to the opening of the hermetic chamber from the outlet is installed, and at least one storage section is provided around the A rotary valve having a rotatable rotor is provided so that the storage section communicates with the opening of the airtight chamber in an airtight manner with rotation, and the drive device rotates the rotary port. This provides a discharge device that continuously discharges the granules.
以上 1¾明 したよ う に構成される本発明に.よれば以下 の効果がある。 According to the present invention configured as described above, the following effects can be obtained.
① 竪型冷却炉の気密を保ちながら粉粒体を連続的 に排出でき るので、 コ ー ク ヮ ー フや シ ー ルホ ッハ0—等 粉粒体を一時的に貯蔵する設備が不要である。 ① while maintaining the airtightness of the vertical cooling furnace can continuously discharge the granular material Runode, co chromatography click Wa over 38628 huya sheet over sulfo Tsu Ha 0 - facilities needed for temporarily storing the equal granular material is there.
② 又、 竪型冷却炉の気密を保つの に二重シ ー ル弁 を使わずに、 ロ ー タ リ ー弁を使用するため、 排出装置 の装置高が低く なる。 従って竪型冷却炉の設備全体が 低く な り設備費が低減される。 (2) In addition, the use of a rotary valve instead of a double seal valve to maintain the airtightness of the vertical cooling furnace reduces the height of the discharge device. Therefore, the entire equipment of the vertical cooling furnace is reduced, and equipment costs are reduced.
以下に本発明の実施例に よ る排出装置を図面に基づ いて説明するが、 これらの説明から本発明の他め面で ある排出方法の特徵も よ り 明瞭となろ う 。 図面の簡単な説明 Hereinafter, a discharge device according to an embodiment of the present invention will be described with reference to the drawings. From these descriptions, characteristics of a discharge method, which is another aspect of the present invention, will be clearer. BRIEF DESCRIPTION OF THE FIGURES
第 1 図は粉粒体用竪型冷却炉の底部に 口 ータ リ 一弁 を設置 した従来の排出装置の例を示す要部断面図、 第 2 図は粉粒体用竪型冷却炉の底部に振動フ ィ ーダ 一を設け、 振動フ ィ ーダ一の排出部に ロ ー タ リ ー弁を 設けた本発明の実施例を示す要部断面図、 Fig. 1 shows a vertical valve at the bottom of a vertical cooling furnace for granular materials. Fig. 2 is a cross-sectional view of an essential part of an example of a conventional discharge device in which a vibration feeder is installed at the bottom of a vertical cooling furnace for granular material. Main part sectional view showing an embodiment of the present invention provided with a rotary valve,
第 3 図は本発明に使用する ロ ー タ リ 一弁の ロ ー タ 一 の斜視図 FIG. 3 is a perspective view of a rotor of a rotary valve used in the present invention.
第 4 図は粉粒体用竪型冷却炉の底部にェ; 7° 口 ン フ ィ ーダ一を設け、 エ フ。 ロ ン フ ィ ーダ一の排出部に ロ ー タ リ ー弁を設けた本発明の他の実施例を示す要部断面図 第 5 図は粉粒体用竪型冷却炉の底部に 口 ー ル フ ィ 一 ダ.一を設け、 ロ ー ルフ ィ ーダ一の排出部に ロ ー タ リ ー 弁を設けた本発明の更に他の実施例を示す要部断面図 、あ 。 発明を実施する ための最良の形態の 開示 Fig. 4 shows a 7 ° port feeder at the bottom of the vertical cooling furnace for powder and granules. FIG. 5 is a sectional view of a main part showing another embodiment of the present invention in which a rotary valve is provided at the discharge part of the feeder. FIG. Fig. 7 is a cross-sectional view of a principal part showing still another embodiment of the present invention in which a feeder is provided and a rotary valve is provided at an outlet of the roll feeder. Disclosure of the best mode for carrying out the invention
第 2 図は竪型冷却炉 1 2 の粉粒体出 口 1 5 下部に気 密室 1 6 を設け、 こ の気密室内に搬送装置であ る振動 フ ィ ーダ一 1 7 を設置 し、 さ ら に こ の振動フ ィ ーダ一 1 7 の排出部に隣接 し て ロ ー タ リ ー弁 1 1 を設けた例 であ る。 図 において、 1 3 は回転可能に設け られた 口 ー タ 一、1 4 はロ ー タ 一 1 3 を収容する ケ ー シ ン グ、 1 8 は ロ ー タ ー羽根であ り ケ ー シ ング 1' 4 の 内周 に摺 動状に接触 し て気密室 1 6 の気密性を保持 し ている。 なお、 本実施例では気密性の保持を ケ ー シ ングと ロ ー タ ー羽根と の直接接触で行っているが、 両者間に シ ー ル手段を介在させて気密性を保持する も のであって も 良い。 Fig. 2 shows an airtight chamber 16 provided below the outlet 15 of the vertical cooling furnace 12 and a vibration feeder 17 as a transfer device installed in the airtight chamber. Further, in this example, a rotor valve 11 is provided adjacent to the discharge section of the vibration feeder 17. In the figure, 13 is a rotatable port, 14 is a casing for accommodating the rotor 13, and 18 is a rotor blade and casing. The inner periphery of 1'4 is slidably contacted with the inner periphery of 1'4, so that the hermeticity of the hermetic chamber 16 is maintained. In this embodiment, the airtightness is maintained by direct contact between the casing and the rotor blades. The airtightness may be maintained by interposing a sealing means.
ロ ー タ ー 1 3 は、 第 3 図に示すよ う に、 気密性を高 め る ために側板 1 9 を設けた も のが よ く 、 振動フ ィ 一 ダー 1 7に よ って連続的かつ定量的に切出 された粉粒体 は ロ ー タ リ ー弁 1 1 への供給口 2 0 に供給され、 ロ ー タ ー羽根 1 8 と 側板 1 9 で ロ ー タ 一 1 3 の周囲に放射 状に形成された複数の収納部に収容され、 さ ら に駆動 装置 ( 図示せず ) に よ る ロ ー タ 一 1 3 の回転に伴って 口 一 タ リ ー弁 1 1 から排出 されて払 出ベ ル ト コ ン べ ャ — 2 1 で運搬される。 As shown in FIG. 3, the rotor 13 is preferably provided with a side plate 19 to improve airtightness, and is continuously provided by a vibrating feeder 17. The granular material cut out quantitatively is supplied to a supply port 20 to a rotor valve 11 and is surrounded by a rotor blade 18 and a side plate 19 around a rotor 13. It is housed in a plurality of storage portions formed radially at the same time, and is further discharged from the mouth-tally valve 11 with the rotation of the rotor 13 by a driving device (not shown). Delivery Belt Conveyor — transported by 21.
振動フ ィ ーダ一 1 7 は、 . .に大きな粒度 ( 2 0 0 籠- 以上 ) 以外は、 定量切出性が良好であ るため、 ロ ー タ 一 羽根 1 8 と 側板 1 9 と で構成される 各空間即ち収納 部に収容能力を超えて供給する こ と が無い よ う に、 即 ち、 満杯と な らない よ う に供給量を制御 し て粒状物を 入れる こ と が可能であ る。 ま た振動 フ ィ ーダ一 1 7 を ロ ー タ リ 一弁 1 1 の上流側に設けた こ と に よ り 、 ロ ー タ リ ー弁 1 1 への供給口 2 0 の開口幅 a に対 し粒状物 の落下流量幅 b を小さ く 取る こ と が可能 と な り 、 ロ ー タ 一羽根 1 8 と ケ ー シ ング 1 4 と の間への粉粒体の みこ みを防止でき る。 The vibratory feeder 17 has a good quantitative cut-out property except for a large particle size (200 baskets or more), so that the rotor 18 and the side plate 19 In order not to supply more than the capacity of each space, that is, the storage unit, it is possible to control the amount of supply so as not to be full, and to add granular materials. is there. In addition, since the vibration feeder 17 is provided upstream of the rotary valve 11, the opening width a of the supply port 20 to the rotary valve 11 is limited. On the other hand, it is possible to make the falling flow width b of the granular material small, and it is possible to prevent the infiltration of the granular material between one rotor blade 18 and the casing 14. .
なお、 振動フ ィ ーダ一 1 7 に よ る切出量と o —タ リ 一弁 1 1 に よ る排出量即ち各収納部の収容能力お よ び π 一タ ー 1 3 の回転速度と の関係等詳細な諸元は、 冷 一 OMPI r 却炉 1 2 の粒状物冷却能力および所望の排出量等から 各々 の設備に応じて定められるべき ものであ り、 こ こ ではこ れ以上詳細な説明を行わない。 In addition, cutting the amount that by the vibration off I over da one 1 7 and the o - the rotational speed of the motor re-Ichiben 1 1 by that emissions ie capacity of each housing unit you good beauty π Ichita-1 3 and Detailed specifications such as the relationship It should be determined according to each facility from the granular cooling capacity of the reactor 12 and the desired discharge amount, etc., and will not be described in further detail here.
又、 供給口 2 0 において粉粒体の落下流にさら され る ロ ータ ー羽根 1 8 の先端部の摩耗が問題とな るが、 振動フ ィ ー ダ一 1 7 に よ って ロ ー タ リ ー弁 1 1 への供 給口 2 0 に供給される粉粒体の落下速度を最小にでき るため、 緩に供給でき ロ ータ ー羽根 1 8 先端部の摩耗 を抑制でき る。 しかも この部分の摩耗は局部的であ り 、 高 c r 錡鉄製等の耐摩材を使用 して も、 口 — タ リ ー弁 1 . -1 全体の設備費用には問題とならない。 更に高いレ ペルの気密性が要本される場合には、 窒.化择素セ ラ ミ ッ ク の如き超耐摩耗材をこ の部分に採用するか、 ある いは取替構造と し、 定期的に取替る よ う に し て高度の 気密性を維持でき る。 Also, there is a problem in that the tip of the rotor blade 18 is exposed to the falling flow of the granular material at the supply port 20, but the vibration feeder 17 causes the rotor blade 18 to wear. Since the falling speed of the granular material supplied to the supply port 20 to the tally valve 11 can be minimized, it can be supplied gently and the rotor blade 18 can be prevented from wearing at the tip. In addition, the wear of this part is local, and even if a high friction material such as high cr steel is used, there is no problem in the overall equipment cost of the port-tally valve 1.1. If a higher level of hermeticity is required, a super abrasion-resistant material such as nitrogen nitride ceramic may be used for this part, or a replacement structure may be used. High airtightness can be maintained by replacing the airtightly.
更に振動フ ィ ーダ一 1 7 は価格も安価で、 耐久性も 十分あ り 実用性が高い。 特に定量切出装置と し て コ ン パク 卜 な点は、 本発明に とって重要であ り、 排出装置 のみならず冷却炉全体を低く でき るの で設備費が低減 される。 Furthermore, the vibration feeder 17 is inexpensive, has sufficient durability, and is highly practical. In particular, the compactness of the quantitative cutout device is important for the present invention, and the equipment cost can be reduced because not only the discharge device but also the entire cooling furnace can be lowered.
しかしながら、 本発明の搬送装置は振動フ ィ ーダ一 に限定される ものではな く 、 本発明の他の実施例と し てエ プ ロ ン フ ィ ーダ一を ロ ー タ リ ー弁—の上流側に定量 切出装置と し て利用する例を第 4図に示す。 However, the transfer device of the present invention is not limited to the vibration feeder, and as another embodiment of the present invention, the epoxy feeder is provided with a rotary valve. Fig. 4 shows an example of using it as a quantitative extraction device upstream of the system.
図において、 1 1 7 は気密室 1 1 6 内に設置された In the figure, 1 17 is installed in the airtight room 1 16
一 OMPI エ プ ロ ン フ ィ ー ダ一で、他の構成部分については第 2 図 に示す実施例の場合と 同様で良 く 、 従って第 2 図の場 合と 同一の符号を付されている。 One OMPI The other components in the epro-feeder are the same as those in the embodiment shown in FIG. 2, and therefore, are denoted by the same reference numerals as in FIG.
ェ ; 7° □ ン フ ィ ーダ一 1 1 7 の特徵は、 大粒度の粉粒 体の切出に対して も 定量切出性がす ぐれてお り 、 定量 切出性 と い う 点では最もす ぐれて いる も の であ るが、 本発明におけ る ロ ー タ リ ー弁 1 1 と の組み合せにおい ては、 供給される粉粒体の流量幅 b を絞るために小さ な シ ュ ー ト 1 1 1 を設け、 ロ ー タ リ —弁 1 1 での粉粒 体のかみ込みを防止する こ とが好ま しい。 °; 7 ° □ The characteristic of the feeder 1-17 is that quantitative extraction is excellent even for the extraction of large-grained powder, and quantitative extraction is easy. In the combination with the rotary valve 11 of the present invention, a small sieve is used to narrow the flow width b of the supplied granular material. It is preferable to provide a cutout 11 1 to prevent the particulates from getting caught in the rotary valve 11.
さ ら,に他の実施例 と し て ό ル フ ィ 一ダ ーを 口 ー タ リ 一弁の上流側 定量切出装置と し て利用する例を第 Further, as another embodiment, an example in which a per-feeder is used as an upstream fixed-quantity extraction device of a single-port valve is described.
5 図に示す。 Figure 5 shows.
図において、 2 1 7 は気密室 2 1 6 内に設置された ロ ー ル フ ィ ーダ一で、 ま た第 2 図お よ び第 4 図 と 同一 の符号は こ れらの図 に示された実施例に用い られる構 成要素 と 同一の も のを示 し ている。 In the figures, reference numeral 217 denotes a roll feeder installed in the hermetic chamber 216, and the same reference numerals as those in FIGS. 2 and 4 denote the same. The same components as those used in the illustrated embodiment are shown.
ロ ー ル フ ィ ーダ一 2 1 7 の特徴は、 構造が簡単で、 耐久性にす ぐれ、 安価であ る点であ る。 ま た前記ェ: 7° ロ ン フ ィ ーダ一 と ロ ー タ リ ー弁と の組合せの場合と 同 様に ロ ー タ リ ー弁 1 1 での粉粒体のかみ 込みを防止す るため、 ロ ー ル フ ィ ーダ一 2 1 7 の排出部に小さな シ ユー ト 2 1 1 を設けた方が よ い。 The characteristics of the Roll Feeder II 17 are that it is simple in structure, durable, and inexpensive. In addition, the same as in the case of the combination of the 7 ° low feeder and the rotary valve, preventing the powder and particulate matter from being caught in the rotary valve 11. For this reason, it is better to provide a small shot 211 at the discharge section of the roll feeder 2 17.
以上本発明を実施例に基づいて説明 したが、 本発明 は こ れら実施例のみに限定される も のでな く 請求の範 囲に示される本発明の概念の範囲内で種々 の変更が可 能であ る こ と は明らかであろ う 。 Although the present invention has been described based on the embodiments, the present invention is not limited to only these embodiments, but rather includes claims. It will be apparent that various modifications are possible within the scope of the inventive concept shown in the box.
OMPI OMPI
Claims
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/JP1984/000448 WO1986001819A1 (en) | 1984-09-17 | 1984-09-17 | Method of and apparatus for discharging pulverulent and granular substance from hermetic vertical cooling furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/JP1984/000448 WO1986001819A1 (en) | 1984-09-17 | 1984-09-17 | Method of and apparatus for discharging pulverulent and granular substance from hermetic vertical cooling furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1986001819A1 true WO1986001819A1 (en) | 1986-03-27 |
Family
ID=13818412
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP1984/000448 Ceased WO1986001819A1 (en) | 1984-09-17 | 1984-09-17 | Method of and apparatus for discharging pulverulent and granular substance from hermetic vertical cooling furnace |
Country Status (1)
| Country | Link |
|---|---|
| WO (1) | WO1986001819A1 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1990010683A1 (en) * | 1989-03-16 | 1990-09-20 | Still Otto Gmbh | Process and device for extracting dry-cooled coke from a coke-quenching tower |
| WO1997046844A1 (en) * | 1996-06-05 | 1997-12-11 | Voest-Alpine Industrieanlagenbau Gmbh | Process for applying sinter material on an already scaled sinter ground coat |
| WO1998054526A1 (en) * | 1997-05-30 | 1998-12-03 | Paul Wurth S.A. | Charging device for a rotary hearth furnace |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5237902A (en) * | 1975-09-20 | 1977-03-24 | Nippon Kokan Kk <Nkk> | Apparatus for discharging coke from quenching chamber of a coke dry qu enching plant |
| JPS5491456U (en) * | 1977-12-09 | 1979-06-28 | ||
| JPS54143705A (en) * | 1978-05-01 | 1979-11-09 | Nagata Seisakusho Co Ltd | Doughnut type rotary cooler |
| JPS5865347U (en) * | 1981-10-27 | 1983-05-02 | 石川島播磨重工業株式会社 | Coke cutting device in coke dry cooling equipment |
-
1984
- 1984-09-17 WO PCT/JP1984/000448 patent/WO1986001819A1/en not_active Ceased
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5237902A (en) * | 1975-09-20 | 1977-03-24 | Nippon Kokan Kk <Nkk> | Apparatus for discharging coke from quenching chamber of a coke dry qu enching plant |
| JPS5491456U (en) * | 1977-12-09 | 1979-06-28 | ||
| JPS54143705A (en) * | 1978-05-01 | 1979-11-09 | Nagata Seisakusho Co Ltd | Doughnut type rotary cooler |
| JPS5865347U (en) * | 1981-10-27 | 1983-05-02 | 石川島播磨重工業株式会社 | Coke cutting device in coke dry cooling equipment |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1990010683A1 (en) * | 1989-03-16 | 1990-09-20 | Still Otto Gmbh | Process and device for extracting dry-cooled coke from a coke-quenching tower |
| WO1997046844A1 (en) * | 1996-06-05 | 1997-12-11 | Voest-Alpine Industrieanlagenbau Gmbh | Process for applying sinter material on an already scaled sinter ground coat |
| WO1998054526A1 (en) * | 1997-05-30 | 1998-12-03 | Paul Wurth S.A. | Charging device for a rotary hearth furnace |
| US6210155B1 (en) | 1997-05-30 | 2001-04-03 | Paul Wurth, S.A. | Charging device for a rotary hearth furnace |
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