JP2012062812A - Waste steam recovery device - Google Patents
Waste steam recovery device Download PDFInfo
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- JP2012062812A JP2012062812A JP2010207413A JP2010207413A JP2012062812A JP 2012062812 A JP2012062812 A JP 2012062812A JP 2010207413 A JP2010207413 A JP 2010207413A JP 2010207413 A JP2010207413 A JP 2010207413A JP 2012062812 A JP2012062812 A JP 2012062812A
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- steam
- vulcanization
- waste
- compression
- waste steam
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- 239000002699 waste material Substances 0.000 title claims abstract description 27
- 238000011084 recovery Methods 0.000 title abstract description 12
- 230000006835 compression Effects 0.000 claims abstract description 19
- 238000007906 compression Methods 0.000 claims abstract description 19
- 238000004073 vulcanization Methods 0.000 abstract description 13
- 238000010438 heat treatment Methods 0.000 abstract description 5
- 238000007599 discharging Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 2
- 238000004378 air conditioning Methods 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
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- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
Description
本発明は、ゴムの加硫缶などの蒸気装置で使用されて残った蒸気を、廃棄するのではなく、再利用できるように回収することのできる廃蒸気回収装置に関する。 The present invention relates to a waste steam recovery apparatus capable of recovering the remaining steam used in a steam apparatus such as a rubber vulcanizing can so that it can be reused instead of being discarded.
廃蒸気回収装置は、蒸気使用装置としてのシュリンクトンネルと、エゼクターと液体タンクと循環ポンプで構成された真空吸引手段とを、廃蒸気回収パイプで接続したもので、シュリンクトンネルからの廃蒸気を真空吸引手段で吸引することによって、モヤモヤと立ち込める廃蒸気を無くすことができるものである。 The waste steam recovery unit is a shrink tunnel that uses steam, and vacuum suction means that consists of an ejector, a liquid tank, and a circulation pump connected by a waste steam recovery pipe. By sucking with the sucking means, it is possible to eliminate waste steam that can get trapped.
この廃蒸気回収装置においては、廃蒸気を液体タンクへ回収するだけであり、廃蒸気を有効に再利用できていない問題があった。 In this waste steam recovery device, there is a problem that the waste steam is only recovered into the liquid tank, and the waste steam cannot be effectively reused.
解決しようとする課題は、蒸気装置からの廃蒸気を有効に再利用することができる廃蒸気回収装置を提供すること。 The problem to be solved is to provide a waste steam recovery device capable of effectively reusing waste steam from a steam device.
本発明は、蒸気装置から蒸気管を介して流下してくる廃蒸気を所定箇所へ排出するものにおいて、蒸気管に蒸気圧縮及び膨張機を配置して、当該蒸気圧縮及び膨張機の圧縮と膨張を切り換える切換弁を取り付けて、当該蒸気圧縮及び膨張機を、発電機及び密閉タンク状の蒸気装置と接続したものである。 In the present invention, waste steam flowing down from a steam device via a steam pipe is discharged to a predetermined location. A steam compression and expansion machine is disposed in the steam pipe, and the compression and expansion of the steam compression and expansion machine are performed. The steam compression and expansion machine is connected to a generator and a closed tank steam device.
本発明の廃蒸気回収装置は、蒸気装置から蒸気を排出する蒸気管に、蒸気圧縮及び膨張機を配置して、発電機及び密閉タンク状の蒸気装置と接続したことによって、蒸気装置に残った廃蒸気が高圧な場合は、蒸気膨張機で膨張させながら発電機で発電させて密閉タンク状の蒸気装置に回収することができ、一方、蒸気装置に残った廃蒸気が低圧な場合は、蒸気圧縮機で低圧蒸気を圧縮して高圧蒸気に変換しながら密閉タンク状の蒸気装置に回収することができる。 The waste steam recovery apparatus of the present invention is left in the steam apparatus by disposing a steam compression and expansion machine in the steam pipe for discharging steam from the steam apparatus and connecting it to the generator and the closed tank steam apparatus. If the waste steam is high pressure, it can be generated by a generator while being expanded by a steam expander and recovered in a closed tank steam device, while if the waste steam remaining in the steam device is low pressure, The low-pressure steam is compressed by a compressor and converted into high-pressure steam, and can be recovered in a sealed tank-like steam device.
本発明の廃蒸気回収装置は、蒸気圧縮及び膨張機を用いるものであるが、この蒸気圧縮及び膨張機としては、冷凍や空調やガスコンプレッサとして従来から幅広く使用されてきたスクリュー式コンプレッサを蒸気圧縮機として用い、一方、蒸気膨張機としては、スクリュー式コンプレッサの逆サイクルを利用することによって、すなわち、スクリュー式コンプレッサの蒸気の入口と出口を逆にして、出口側から高圧蒸気を注入し、入口側から膨張して圧力の低下した低圧蒸気を流下させることによって蒸気膨張機として用いることができる。更に、従来周知の蒸気コンプレッサを蒸気圧縮機として用い、その逆サイクルを蒸気膨張機として用いることもできる。 The waste steam recovery apparatus of the present invention uses a steam compressor and expander. As the steam compressor and expander, a screw compressor that has been widely used for refrigeration, air conditioning, and gas compressors has been steam-compressed. On the other hand, as a steam expander, by utilizing the reverse cycle of the screw compressor, that is, by reversing the steam inlet and outlet of the screw compressor, high pressure steam is injected from the outlet side, and the inlet It can be used as a steam expander by letting low-pressure steam expanded from the side and having a reduced pressure flow down. Furthermore, a conventionally well-known steam compressor can be used as a steam compressor, and its reverse cycle can be used as a steam expander.
図1において、蒸気装置としてのゴムの加硫缶1と、加硫缶1へ加熱用の蒸気を供給する加熱蒸気供給管2と、加硫缶1から残った蒸気を排出する蒸気管3と、蒸気圧縮及び膨張機4、及び、密閉タンク状の蒸気装置5とで本発明の廃蒸気回収装置を構成する。 In FIG. 1, a rubber vulcanizing can 1 as a steam device, a heating steam supply pipe 2 for supplying steam for heating to the vulcanizing can 1, and a steam pipe 3 for discharging steam remaining from the vulcanizing can 1 The steam compression and expansion machine 4 and the closed tank steam device 5 constitute the waste steam recovery device of the present invention.
加硫缶1から残った蒸気を排出する蒸気管3には、蒸気圧縮及び膨張機4での圧縮と膨張を切り換える複数の切換弁6,7,8,9,10,11を配置して、それぞれの切換弁に応じた切換管路を形成する。 In the steam pipe 3 for discharging the steam remaining from the vulcanizing can 1, a plurality of switching valves 6, 7, 8, 9, 10, and 11 for switching between compression and expansion in the steam compression and the expander 4 are arranged, A switching line corresponding to each switching valve is formed.
蒸気管3の切換弁7の下方に蒸気圧縮及び膨張機4を接続する。本実施例においては、スクリュー式蒸気圧縮及び膨張機4を用いた例を示す。スクリュー式蒸気圧縮及び膨張機4は、左右一対のオス・メスのスクリュー式ロータ部12、及び、発電機13とで構成する。 A steam compression and expansion machine 4 is connected below the switching valve 7 of the steam pipe 3. In this embodiment, an example using a screw type vapor compression and expansion machine 4 is shown. The screw type vapor compression and expansion machine 4 is composed of a pair of left and right male and female screw type rotor parts 12 and a generator 13.
加熱蒸気供給管2から加硫缶1へ供給される蒸気によって、加硫缶1内部の図示しないゴムが加硫されるものである。加硫が終了して加硫缶1に残った蒸気が高圧な場合は、切換弁6,7,8,9を開弁して、高圧蒸気をスクリュー式ロータ部12の左側から供給することで、高圧蒸気がスクリュー式ロータ部12を回転させながら膨張し、減圧されて密閉タンク状の蒸気装置5へ供給され回収される。この場合、スクリュー式ロータ部12の回転駆動力は、連結された発電機13を回転させて所定の電力を発生する。 The rubber (not shown) inside the vulcanizing can 1 is vulcanized by the steam supplied from the heating steam supply pipe 2 to the vulcanizing can 1. When the vulcanization is completed and the steam remaining in the vulcanizing can 1 is at a high pressure, the switching valves 6, 7, 8, and 9 are opened to supply the high-pressure steam from the left side of the screw-type rotor unit 12. The high-pressure steam expands while rotating the screw-type rotor unit 12, is decompressed, and is supplied to the steam device 5 in a sealed tank shape and recovered. In this case, the rotational driving force of the screw-type rotor unit 12 rotates the connected generator 13 to generate predetermined power.
一方、加硫缶1内の蒸気圧力が密閉タンク状の蒸気装置5内の蒸気圧力よりも低下した場合は、切換弁6,10,8,7,11を開弁して、低圧蒸気をスクリュー式ロータ部12の右側から、すなわち、上述の減圧膨張する場合とは逆方向からスクリュー式ロータ部12へ供給することで、スクリュー式ロータ部12が、発電機13に内蔵した図示しない電動モータによって回転駆動され、低圧蒸気は圧縮されて所定圧まで昇圧して、密閉タンク状の蒸気装置5へ供給され回収される。このようにして、加硫缶1内の高圧から低圧までの蒸気は、所定圧力となって密閉タンク状の蒸気装置5に回収されるものである。なお、密閉タンク状の蒸気装置5で必要とする蒸気量が不足する場合は、蒸気補給管14から不足分の蒸気を供給することができる。 On the other hand, when the steam pressure in the vulcanizing can 1 is lower than the steam pressure in the closed tank steam device 5, the switching valves 6, 10, 8, 7, 11 are opened and the low pressure steam is screwed. By supplying the screw rotor unit 12 from the right side of the rotor unit 12 from the right side, that is, from the direction opposite to the above-described decompression and expansion, the screw rotor unit 12 is driven by an electric motor (not shown) built in the generator 13. Driven by rotation, the low-pressure steam is compressed and boosted to a predetermined pressure, and is supplied to the sealed tank-like steam device 5 and collected. In this way, the steam from the high pressure to the low pressure in the vulcanizing can 1 becomes a predetermined pressure and is collected in the closed tank steam device 5. In addition, when the amount of steam required by the sealed tank steam device 5 is insufficient, the insufficient amount of steam can be supplied from the steam supply pipe 14.
加硫缶1で再度、加硫を実施する場合は、まず、密閉タンク状の蒸気装置5へ回収された所定圧力の廃蒸気を、切換弁11,7,8,10,6を開弁して、スクリュー式ロータ部12の左側から供給することで、蒸気がスクリュー式ロータ部12を回転させながら膨張し、減圧されて加硫タンク1へ供給される。この場合も、スクリュー式ロータ部12の回転駆動力は、連結された発電機13を回転させて所定の電力を発生する。 When the vulcanization can be performed again with the vulcanizing can 1, first, the switching valve 11, 7, 8, 10, 6 is opened for the waste steam of a predetermined pressure recovered to the closed tank steam device 5. By supplying from the left side of the screw type rotor unit 12, the steam expands while rotating the screw type rotor unit 12, is decompressed, and is supplied to the vulcanization tank 1. Also in this case, the rotational driving force of the screw-type rotor unit 12 rotates the connected generator 13 to generate predetermined power.
密閉タンク状の蒸気装置5内の蒸気圧力が、加硫缶1内の蒸気圧力よりも低下してくると、切換弁9,8,7,6を開弁して、低圧蒸気をスクリュー式ロータ部12の右側からスクリュー式ロータ部12へ供給することで、スクリュー式ロータ部12が、電動モータによって回転駆動され、低圧蒸気は圧縮されて所定圧まで昇圧して、加硫缶1へ供給される。このようにして、加硫缶1から密閉タンク状の蒸気装置5へ回収された廃蒸気は、再度、加硫缶1へ供給されることで、廃蒸気が有効に再利用される。 When the steam pressure in the closed tank steam device 5 becomes lower than the steam pressure in the vulcanizing can 1, the switching valves 9, 8, 7, 6 are opened, and the low pressure steam is supplied to the screw rotor. By supplying the screw-type rotor unit 12 from the right side of the unit 12, the screw-type rotor unit 12 is rotationally driven by the electric motor, and the low-pressure steam is compressed to a predetermined pressure and supplied to the vulcanizing can 1. The In this way, the waste steam recovered from the vulcanization can 1 to the closed tank steam device 5 is supplied again to the vulcanization can 1 so that the waste steam is effectively reused.
加硫缶1で必要とする蒸気が密閉タンク状の蒸気装置5から供給できなくなると、加熱蒸気供給管2から必要とする蒸気を加硫缶1へ供給することで、加硫を継続して実施することができる。 When the steam required by the vulcanizing can 1 can no longer be supplied from the closed tank steam device 5, vulcanization is continued by supplying the required steam from the heated steam supply pipe 2 to the vulcanizing can 1. Can be implemented.
本発明は、多量の蒸気を間欠的に使用する各種蒸気使用装置における、廃蒸気回収装置として利用することができる。 INDUSTRIAL APPLICABILITY The present invention can be used as a waste steam recovery device in various steam using devices that intermittently use a large amount of steam.
1 加硫缶
2 加熱蒸気供給管
3 蒸気管
4 蒸気圧縮及び膨張機
5 密閉タンク状の蒸気装置
6,7,8,9,10,11 切換弁
12 スクリュー式ロータ部
13 発電機
DESCRIPTION OF SYMBOLS 1 Vulcanization can 2 Heating steam supply pipe 3 Steam pipe 4 Steam compression and expansion machine 5 Sealed tank-like steam device 6, 7, 8, 9, 10, 11 Switching valve 12 Screw-type rotor part 13 Generator
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JP2010207413A JP5627970B2 (en) | 2010-09-16 | 2010-09-16 | Waste steam recovery device |
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JP2010207413A JP5627970B2 (en) | 2010-09-16 | 2010-09-16 | Waste steam recovery device |
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JP5627970B2 JP5627970B2 (en) | 2014-11-19 |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2012063068A (en) * | 2010-09-16 | 2012-03-29 | Tlv Co Ltd | Exhaust steam recovery device |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62127210A (en) * | 1985-11-29 | 1987-06-09 | Mitsubishi Heavy Ind Ltd | Gas vulcanization of rubber tire and the like |
JPS63221018A (en) * | 1987-03-10 | 1988-09-14 | Bridgestone Corp | Vulcanization of tire |
JPS63277436A (en) * | 1987-05-06 | 1988-11-15 | Nippon Steel Corp | Buffer storage system for power generation gas |
JPH10227203A (en) * | 1997-02-14 | 1998-08-25 | Toyota Auto Body Co Ltd | Cogeneration system |
JP2001021273A (en) * | 1999-07-09 | 2001-01-26 | Nippon Steel Corp | Method for leveling load in high pressure steam condensor of waste processing facility and device for leveling load |
JP2002005582A (en) * | 2000-06-19 | 2002-01-09 | Tlv Co Ltd | Heat exchange waste steam recoverer |
JP2003065621A (en) * | 2001-08-24 | 2003-03-05 | Shimadzu Corp | Cooling system |
JP2008019813A (en) * | 2006-07-14 | 2008-01-31 | Tlv Co Ltd | Control device of process steam |
JP2008019811A (en) * | 2006-07-14 | 2008-01-31 | Tlv Co Ltd | Control device of process steam |
-
2010
- 2010-09-16 JP JP2010207413A patent/JP5627970B2/en not_active Expired - Fee Related
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62127210A (en) * | 1985-11-29 | 1987-06-09 | Mitsubishi Heavy Ind Ltd | Gas vulcanization of rubber tire and the like |
JPS63221018A (en) * | 1987-03-10 | 1988-09-14 | Bridgestone Corp | Vulcanization of tire |
JPS63277436A (en) * | 1987-05-06 | 1988-11-15 | Nippon Steel Corp | Buffer storage system for power generation gas |
JPH10227203A (en) * | 1997-02-14 | 1998-08-25 | Toyota Auto Body Co Ltd | Cogeneration system |
JP2001021273A (en) * | 1999-07-09 | 2001-01-26 | Nippon Steel Corp | Method for leveling load in high pressure steam condensor of waste processing facility and device for leveling load |
JP2002005582A (en) * | 2000-06-19 | 2002-01-09 | Tlv Co Ltd | Heat exchange waste steam recoverer |
JP2003065621A (en) * | 2001-08-24 | 2003-03-05 | Shimadzu Corp | Cooling system |
JP2008019813A (en) * | 2006-07-14 | 2008-01-31 | Tlv Co Ltd | Control device of process steam |
JP2008019811A (en) * | 2006-07-14 | 2008-01-31 | Tlv Co Ltd | Control device of process steam |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012063068A (en) * | 2010-09-16 | 2012-03-29 | Tlv Co Ltd | Exhaust steam recovery device |
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