JPH01315690A - Dry type screw compressor incorporated with exhaust heat recovery device - Google Patents
Dry type screw compressor incorporated with exhaust heat recovery deviceInfo
- Publication number
- JPH01315690A JPH01315690A JP14572488A JP14572488A JPH01315690A JP H01315690 A JPH01315690 A JP H01315690A JP 14572488 A JP14572488 A JP 14572488A JP 14572488 A JP14572488 A JP 14572488A JP H01315690 A JPH01315690 A JP H01315690A
- Authority
- JP
- Japan
- Prior art keywords
- aqueous solution
- recovery device
- cooling
- water
- compressor
- 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
Links
- 238000011084 recovery Methods 0.000 title claims description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 36
- 239000007864 aqueous solution Substances 0.000 claims description 25
- 239000002918 waste heat Substances 0.000 claims description 14
- 238000001816 cooling Methods 0.000 claims description 13
- 239000002826 coolant Substances 0.000 claims description 4
- 238000007710 freezing Methods 0.000 claims description 4
- 230000008014 freezing Effects 0.000 claims description 4
- 208000028659 discharge Diseases 0.000 description 13
- 239000000498 cooling water Substances 0.000 description 9
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 6
- 239000003921 oil Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 241001474791 Proboscis Species 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Applications Or Details Of Rotary Compressors (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、廃熱回収装置付き乾式スクリュー圧縮機に係
り、特に良質な冷却水が得られない場合であっても、効
果的に熱回収を行うために好適なPA廃熱回収装置付乾
式スクリュー圧縮機に関する〔従来の技術〕
冷却に使用した後の温排水の保有熱を利用する従来技術
としては、′#開昭50−150949号公報に記載の
よりに、冷却媒体としての冷却水は密閉強制循環ではな
く、冷却水を補給するようになっている。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a dry screw compressor with a waste heat recovery device, which can effectively recover heat even when high-quality cooling water is not available. [Conventional technology] Regarding a dry screw compressor with a PA waste heat recovery device suitable for carrying out the following: As a conventional technology that utilizes the retained heat of heated waste water after being used for cooling, there is a conventional technology disclosed in '# 150949/1983. As described in , the cooling water as a cooling medium is not circulated in a closed forced circulation, but is supplied with cooling water.
冷却を必要とする乾式スクリュー圧縮機では、冷却に夏
用する水質が悪いと、腐食によって発生する錆やスラツ
ジにより、冷却器が早期rζ目、債まりを起こすなど、
圧縮機のメンデナンス上での問題がありた。For dry screw compressors that require cooling, if the quality of the water used for cooling in the summer is poor, rust and sludge generated by corrosion may cause premature failure of the cooler and cause problems.
There was a problem with the maintenance of the compressor.
また、冷却媒体に移された乾式スクリュー圧縮機の廃熱
は、そのまま排出されているのが現状でめる。Furthermore, the waste heat from the dry screw compressor that is transferred to the cooling medium is currently being discharged as is.
本発明の目的は、良質な冷却水が得らnない場合におい
ても、充分な冷却が行われ、圧縮機からの廃熱が温水お
よび尚温水として回収が可能な廃熱回収装置付き乾式ス
クリュー圧縮機を提供することにある。The object of the present invention is to provide a dry screw compressor equipped with a waste heat recovery device that can perform sufficient cooling even when high-quality cooling water is not available, and can recover waste heat from the compressor as hot water or still hot water. The aim is to provide the opportunity.
前記目的は、例えばプロピレングリコールを主成分とす
る凍結温度が低くかつ腐實性の弱い無公害の水溶液を冷
却媒体としてウォータポンプにより二系統に分けて強制
循環させるとともに、この水溶液との熱交換により圧M
E磯の廃熱を温水および高温水として回収する熱交換器
を設けたことにより、達成さ几る。The purpose is, for example, to forcibly circulate a non-polluting aqueous solution containing propylene glycol as a main component with a low freezing temperature and weak corrosiveness as a cooling medium in two systems using a water pump, and by exchanging heat with this aqueous solution. Pressure M
This is achieved by installing a heat exchanger that recovers waste heat from E-iso as hot water and high-temperature water.
本発明では、ウォータポンプにより、凍結温度が低くか
つ腐夾性の弱い無公害の水溶液を、密閉状態で二系統e
こ分けて強rli′II循咳させ、汚rty、−増加さ
せる吻質が外部から入ることを防止している。In the present invention, a water pump is used to supply a non-polluting aqueous solution with a low freezing temperature and weak corrosivity to two systems in a sealed state.
It separates the throat and causes strong rli'II circulation, preventing the proboscis from entering from the outside.
そして、二系統のうちの一つの系統で11冷却を必要と
する空気冷却器や油冷却器およびジャケット付きケーシ
ングの冷却を行い、もう一つの系統でV′i1次′1j
tlI空気冷却器の冷却を行つ。Then, one of the two systems cools the air cooler, oil cooler, and jacketed casing that require 11 cooling, and the other system cools the V′i primary′1j
tlI air cooler cooling.
また、温くなった水溶液2よび高温となった水溶液との
熱交換器を設けることにより、水溶液に移された圧縮機
の廃熱を温水および高温水とじて回収することが出来る
。Further, by providing a heat exchanger between the warmed aqueous solution 2 and the high temperature aqueous solution, the waste heat of the compressor transferred to the aqueous solution can be recovered as hot water and high temperature water.
以−ド、不発明の実施例を第1図により説明するこの第
1図に示す実施例の廃熱回収装置付き乾式スクリュー圧
縮機Vま、エアフィルタlと、低圧段側圧縮機本体2と
、高圧段側圧縮機本体3と、中間段1次91!I空気冷
却器舎と、中間段空気冷却器5と、吐出段1次側空気冷
却器6と、吐出段空気冷却器7と、油冷却器8と、吐出
空気逆止弁9と、ウォータポンプ10と、水溶f夜タン
ク11と、水溶液流量調整弁12と、温水回収器13と
、高温水回収器lΦとを備えて構成されている。Hereinafter, an uninvented embodiment will be explained with reference to FIG. 1. The dry screw compressor V with a waste heat recovery device, the air filter I, and the low-pressure stage compressor main body 2 of the embodiment shown in FIG. , the high-pressure stage side compressor main body 3, and the intermediate stage primary 91! I air cooler house, intermediate stage air cooler 5, discharge stage primary air cooler 6, discharge stage air cooler 7, oil cooler 8, discharge air check valve 9, water pump 10, an aqueous solution tank 11, an aqueous solution flow rate adjustment valve 12, a hot water recovery device 13, and a high temperature water recovery device lΦ.
前記温水回収器18には冷却水給水口1t5と温水排出
口17の組が設けられており、高温水回収器14には冷
却水給水口18と高温水排出口19の組が設けらfL−
(いる。The hot water recovery device 18 is provided with a set of a cooling water supply port 1t5 and a hot water discharge port 17, and the high temperature water recovery device 14 is provided with a set of a cooling water supply port 18 and a high temperature water discharge port 19.
(There is.
前記実施例のg3熱回収装置付き乾式スクリュー圧縮機
は、次のように運転され、作用する。The G3 dry screw compressor with heat recovery device of the above embodiment is operated and functions as follows.
エアフィルタ1により清浄化さt”tた空気は、低圧段
側圧縮機本体2により中間圧まで圧縮され、中間段l−
次側空気冷却器4および中間段空気冷却器5により冷却
された後に、高圧段側圧縮機本体8に入り、吐出圧力ま
で圧縮され、吐出空気逆上弁9を経て吐出段1次側空気
冷却器6および吐出段空気冷却器7により冷却され、吐
出口15よりプロセスへ圧送される。The air purified by the air filter 1 is compressed to an intermediate pressure by the low-pressure stage compressor main body 2, and then
After being cooled by the next side air cooler 4 and the intermediate stage air cooler 5, it enters the high pressure stage side compressor main body 8, is compressed to the discharge pressure, and passes through the discharge air reverse valve 9 to cool the discharge stage primary side air. It is cooled by the container 6 and the discharge stage air cooler 7, and is then pumped through the discharge port 15 to the process.
中間段1次側空気冷却器42よび吐出段1次側空気冷却
器6へは、zoo’c程度の高温空気が入り、これを冷
却した後に、中間段空気冷却器5および吐出段空気冷却
器7により空気温度を45゛c程度まで冷却する。High-temperature air of approximately zoo'c enters the intermediate stage primary air cooler 42 and the discharge stage primary air cooler 6, and after cooling it, the intermediate stage air cooler 5 and the discharge stage air cooler 6 enter the intermediate stage primary air cooler 42 and the discharge stage primary air cooler 6. 7 to cool the air temperature to about 45°C.
また、油冷却器8は圧縮機本体の軸受や歯車へ給油され
、排出さ几た潤滑油を冷却するもので、低圧段側圧ls
@本体2および高圧段側圧縮機本体3ri高温となるた
め、ジャケット付きケーシングにより冷却するようにな
っている。In addition, the oil cooler 8 cools the lubricating oil that is supplied to the bearings and gears of the compressor body and is discharged.
Since the main body 2 and the high-pressure stage side compressor main body 3ri reach high temperatures, they are cooled by a jacketed casing.
水溶液タンク11内にある、例えばプロピレングリコー
ルを主成分とする凍結温度が低くかつ腐食性の弱い無公
害の水溶液は、ウォータポンプlOKより二つの系統に
分けて強制循環される。A non-polluting aqueous solution containing propylene glycol as a main component, which has a low freezing temperature and is weakly corrosive, in the aqueous solution tank 11 is forcibly circulated into two systems by a water pump lOK.
その一つの系統では、水溶液は吐出段窒気冷却器7、中
間段空気冷却器5および油冷却68に送らnて冷却を行
い、前記油冷却器8へ送られた水溶液は、高圧段側圧縮
機本体3′s?よび低圧段側圧WI機本体2のジャケッ
トを冷却し、合流したうえ、排出される。In one system, the aqueous solution is sent to the discharge stage nitrogen cooler 7, the intermediate stage air cooler 5 and the oil cooler 68 for cooling, and the aqueous solution sent to the oil cooler 8 is compressed on the high pressure stage side. Aircraft body 3's? and the jacket of the lateral pressure WI machine body 2 of the low-pressure stage are cooled, merged, and then discharged.
もウ一つの系統では、水溶液は水溶液流量調整弁12に
より、高温水として回収出来るように流量調整され、吐
出段1次側空気冷却器6および中間段1次1ill空気
冷却54に送られ、高温状態での熱回収冷却を行い、合
流したうえ、排出される。In one system, the flow rate of the aqueous solution is adjusted by the aqueous solution flow rate adjustment valve 12 so that it can be recovered as high-temperature water, and the aqueous solution is sent to the primary side air cooler 6 of the discharge stage and the primary 1ill air cooler 54 of the intermediate stage. The heat is recovered and cooled, and then it is combined and discharged.
圧縮器の廃熱を受は取った水溶液は、温水回収!13お
よび高温水回収器14により冷却され、水溶液タンク1
1へ戻る。冷却水は、冷却水給水口16および18から
温水回収器18および高温水回収器14へ入り、圧m機
の廃熱を回収し、温水排出口17および高温水排出口1
9がら排出される。The aqueous solution that has received the waste heat from the compressor is recovered as hot water! 13 and a high temperature water recovery device 14, the aqueous solution tank 1
Return to 1. The cooling water enters the hot water recovery device 18 and the high temperature water recovery device 14 from the cooling water supply ports 16 and 18, recovers the waste heat of the pressurizer, and passes through the hot water outlet 17 and the high temperature water outlet 1.
9 pieces are discharged.
この実施例によれば、良質な冷却水が得らf′Lない場
合においても、次分な冷却が行われるとともに、圧縮機
からの廃熱を温水および高温水として回収することが出
来る。According to this embodiment, even if good quality cooling water is not available f'L, further cooling can be performed and waste heat from the compressor can be recovered as hot water and high temperature water.
以上説明した本発明によれば、ウォータポンプにより、
凍結製置が低くかつ腐食性の弱い無公害の水溶液を、密
閉状態で二系統に分けて強制循環させ、汚れを増加させ
る+WJ實が外部から入ること防止し、二系統のうちの
一つの系統では冷却を必要とする空気冷却器や油冷却器
り一よびジャケット付きケーシングの冷却を行い、もう
一つの系統では1次1llll仝気冷却器の冷却を行う
とともに、温くなった水溶液および高温となった水溶液
との熱交換器を設けることにより、水溶液に移された圧
縮機の廃熱を温水pよび高温水として回収することが出
来るので、浴用−?温水プールなどの加熱源や暖房用の
補助熱源等への利用が可能となり、省エネルギー化を図
ることが出来るという効果があるAccording to the present invention described above, the water pump
A non-polluting aqueous solution with low freeze production and weak corrosiveness is forcedly circulated in two systems in a sealed state to prevent +WJ material from entering from the outside, which increases contamination, and one of the two systems is In one system, the air cooler, oil cooler, and jacketed casing that require cooling are cooled, and in the other system, the primary air cooler is cooled, and the heated aqueous solution and high temperature are cooled. By providing a heat exchanger with the aqueous solution, the waste heat from the compressor transferred to the aqueous solution can be recovered as hot water and high-temperature water. It can be used as a heating source for hot water pools, etc., or as an auxiliary heat source for heating, and has the effect of saving energy.
第1図は本発明の一実施例を示す系統図である2・・・
低圧段測圧縮機本体 3・・・高圧段側圧縮機本体
慟・・・中間段1次側空気冷却器 5・・・中間段
空気冷却6 6・・・吐出段1次側空気冷却器 7・
・・吐出段仝気冷却! 10・・・ウォータポンプ
11・・・水溶液タンク 13・・・温水回収a
14・・・高温水回収器。
代理人升理士 小 川 勝 橘−7′FIG. 1 is a system diagram showing one embodiment of the present invention.
Low pressure stage compressor body 3... High pressure stage side compressor body
5. Intermediate stage primary air cooler 5. Intermediate stage air cooling 6 6. Discharge stage primary air cooler 7.
・Discharge stage air cooling! 10...Water pump 11...Aqueous solution tank 13...Hot water recovery a
14...High temperature water recovery device. Agent Masaru Masaru Ogawa Tachibana-7'
Claims (1)
ケット付きケーシングを有する乾式スクリュー圧縮機に
おいて、凍結温度が低くかつ腐食性の弱い無公害の水溶
液を冷却媒体としてウォータポンプにより二系統に分け
て強制循環させるとともに、この水溶液との熱交換によ
り圧縮機の廃熱を温水および高温水として回収する熱交
換器を設けたことを特徴とする廃熱回収装置付き乾式ス
クリュー圧縮機。1. In dry screw compressors with air coolers, oil coolers, and jacketed casings that require cooling, water pumps are used to separate the systems into two systems using a non-polluting aqueous solution with a low freezing temperature and low corrosivity as the cooling medium. 1. A dry screw compressor with a waste heat recovery device, characterized in that a heat exchanger is provided for forcing circulation through the aqueous solution and recovering the waste heat of the compressor as hot water and high-temperature water by heat exchange with the aqueous solution.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14572488A JPH01315690A (en) | 1988-06-15 | 1988-06-15 | Dry type screw compressor incorporated with exhaust heat recovery device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14572488A JPH01315690A (en) | 1988-06-15 | 1988-06-15 | Dry type screw compressor incorporated with exhaust heat recovery device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01315690A true JPH01315690A (en) | 1989-12-20 |
Family
ID=15391666
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14572488A Pending JPH01315690A (en) | 1988-06-15 | 1988-06-15 | Dry type screw compressor incorporated with exhaust heat recovery device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01315690A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2017111120A1 (en) * | 2015-12-25 | 2017-06-29 | 株式会社日立産機システム | Gas compressor |
-
1988
- 1988-06-15 JP JP14572488A patent/JPH01315690A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2017111120A1 (en) * | 2015-12-25 | 2017-06-29 | 株式会社日立産機システム | Gas compressor |
JPWO2017111120A1 (en) * | 2015-12-25 | 2018-05-24 | 株式会社日立産機システム | Gas compressor |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0736161B1 (en) | An air cooling system | |
US4745768A (en) | Combustion-powered refrigeration with decreased fuel consumption | |
US4693736A (en) | Oil cooled hermetic compressor used for helium service | |
JPH01315690A (en) | Dry type screw compressor incorporated with exhaust heat recovery device | |
JPH01170788A (en) | Dry-type screw compressor having exhaust heat recovery device | |
JPS5932765A (en) | Heat pump system | |
WO2021196770A1 (en) | Integrated mast comprehensive cooling system | |
JPH03172584A (en) | Dry compressed air feeder | |
JP2796342B2 (en) | Dry compressed air supply device | |
CN212028242U (en) | Hydraulic oil refrigerator | |
JPS6343663B2 (en) | ||
CN220958987U (en) | Dual-drive cooled air energy heat pump | |
CN105674612B (en) | A kind of freon/CO2Overlapping prizes block set type refrigeration system | |
SU1362850A2 (en) | Mine air-conditioning plant | |
JPS60111092A (en) | Cooling method of compressed gas in gas compressor plant equipped with power recovering apparatus | |
JP4314131B2 (en) | Cooling mechanism for engine-driven oil-free compressor | |
CN214171021U (en) | Hydraulic oil circulative cooling system | |
KR100574275B1 (en) | Wastewater Heat Recovery System Using Freezer | |
CN216767542U (en) | Intelligent circulation main body | |
CN219693611U (en) | Military air conditioner refrigerating system capable of refrigerating in large temperature area | |
CN210036383U (en) | Swimming pool water system with condensation waste heat auxiliary heating function of water chilling unit | |
CN86104578A (en) | Reverse-flow type ice maker-heat pump combined operating technology and equipment thereof | |
JPS61108801A (en) | Waste heat recovery system | |
JPS57198942A (en) | Air conditioner | |
JPS6166060A (en) | Engine-heat pump device |