CN101017040A - Exhaust gas heat exchanger used in ammonia water absorption refrigeration device using residual heat of exhaust gas - Google Patents
Exhaust gas heat exchanger used in ammonia water absorption refrigeration device using residual heat of exhaust gas Download PDFInfo
- Publication number
- CN101017040A CN101017040A CNA2007100269944A CN200710026994A CN101017040A CN 101017040 A CN101017040 A CN 101017040A CN A2007100269944 A CNA2007100269944 A CN A2007100269944A CN 200710026994 A CN200710026994 A CN 200710026994A CN 101017040 A CN101017040 A CN 101017040A
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- CN
- China
- Prior art keywords
- tail gas
- heat exchanger
- waste heat
- water absorption
- refrigeration device
- 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.)
- Granted
Links
- 238000005057 refrigeration Methods 0.000 title claims description 26
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 title claims description 21
- 235000011114 ammonium hydroxide Nutrition 0.000 title claims description 21
- 238000010521 absorption reaction Methods 0.000 title claims description 14
- 239000007788 liquid Substances 0.000 claims abstract description 36
- 239000007789 gas Substances 0.000 claims description 58
- 239000002918 waste heat Substances 0.000 claims description 46
- 238000009434 installation Methods 0.000 claims description 2
- 230000002093 peripheral effect Effects 0.000 claims description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract description 34
- 229910021529 ammonia Inorganic materials 0.000 abstract description 17
- 238000001179 sorption measurement Methods 0.000 abstract 3
- 238000010438 heat treatment Methods 0.000 description 5
- 239000006096 absorbing agent Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Abstract
The invention discloses a tail gas heat exchanger used in ammonia adsorption refrigerator which can utilize the left heat of tail gas. The invention can supply stable heat to the left-heat refrigerator, while the heat exchanger uses external structure to be maintained easily. Based on the ammonia adsorption refrigerator, the invention connects a tail gas heat exchanger on a gas-liquid entrance of a left-heat generator as tubular frame steam generator, and a gas-liquid separator between the tail gas heat exchanger and the left-heat generator. The invention can be used on the ammonia adsorption refrigerator on ship or engine.
Description
Technical field
The present invention relates to ammonia-water absorption-type refrigeration device, particularly utilize the tail gas heat exchanger of the used in ammonia water absorption refrigeration device of using waste heat from tail gas.
Background technology
It is the patent application document of CN2842312 that the Chinese patent communique discloses publication number, the refrigerating plant that this patent application document is described can utilize the using waste heat from tail gas of engine to realize the refrigeration requirement, has higher coefficient of refrigerating performance, and volume, weight are less, can be applicable to such as on automobile, this class means of transport of fishing boat.The described ammonia-water absorption-type refrigeration device that utilizes using waste heat from tail gas of above-mentioned patent application document, comprise waste heat generator, rectifier, regenerator, solution choke valve, liquefied ammonia choke valve, evaporimeter, solution pump, condenser, absorber, generation-absorption heat exchanger, carry and heat up in a steamer device and return cooler, constitute the closed circuit of ammonia spirit and the closed circuit of ammonia by being connected respectively.
The waste heat generator of this device adopts the shell-tube type structure, is made up of drum tank body and one group of tubulation.Tail gas is directly walked tube side, by carrying out heat exchange with the ammonia spirit that circulates in device of walking shell side, thereby realizes utilizing the process of refrigerastion of using waste heat from tail gas.
Though above-mentioned waste heat generator is a relatively independent structure,, when the waste heat generator breaks down, damages or reaches service life, be not easy to maintenance or replacing because it is installed within the integral body of refrigerating plant.But also because this waste heat generator adopts the direct-fired form of tail gas, and the running status of engine usually is unsettled (especially in the operation and means of transport of fishing boat one class), as the start-stop of machine, the variation of load power etc., all directly influence the heat energy that tail gas produces at any time, comprise that air demand changes greatly, exhaust temperature fluctuates greatly, like this, just be unfavorable for utilizing very much stable, the continuous and operate as normal of heat refrigeration apparatus.
Summary of the invention
The object of the present invention is to provide the tail gas heat exchanger of the used in ammonia water absorption refrigeration device that utilizes using waste heat from tail gas of a kind of convenient for maintaining and replacing, it can be to utilizing heat refrigeration apparatus that the heat energy of temperature stabilization, heating load equilibrium is provided, and is beneficial to utilize the stable, continuously and operate as normal of heat refrigeration apparatus.
Technical solution proposed by the invention is such: a kind of tail gas heat exchanger of utilizing the used in ammonia water absorption refrigeration device of using waste heat from tail gas, comprise the waste heat generator that is installed in the described ammonia-water absorption-type refrigeration device, import and export the tail gas heat exchanger that is connected to peripheral hardware in the shell side vapour-liquid of described waste heat generator.
Described tail gas heat exchanger is a steam generator, adopt tube shell type structure, tail gas is walked tube side, steam is walked shell side, also be provided with vapour liquid separator between tail gas heat exchanger and waste heat generator, tail gas heat exchanger shell side top is connected with the steam inlet of vapour liquid separator, and tail gas heat exchanger shell side bottom is connected by liquid back pipe with the vapour liquid separator bottom, the top of vapour liquid separator is connected with waste heat generator shell side top, and waste heat generator shell side bottom is connected with liquid back pipe.In the row tube bundle in the tail gas heat exchanger, all be carved with thread groove on the every tubulation tube wall.The installation site of requirement tail gas heat exchanger is lower than the waste heat generator in the ammonia-water absorption-type refrigeration device.
Compared with prior art, the present invention has following remarkable result:
(1) because tail gas heat exchanger is external in ammonia-water absorption-type refrigeration device, and mostly under the situation, fault and damaging all occurs on the tail gas heat exchanger, safeguards and replacing so greatly facilitate.
(2) key technology of the present invention is that using waste heat from tail gas converts working medium to by heat exchanger high-temperature steam carries out indirect to ammonia-water absorption-type refrigeration device, because it is comparatively steady that vapor (steam) temperature changes, heating load is also more stable, thereby, help utilizing ammonia-water absorption-type refrigeration device stable, continuously and operate as normal of using waste heat from tail gas.
(3) owing to the form that has adopted the tail gas indirect heating, thereby, of the direct input of power heat energy avoided, the security that has improved this refrigerating plant to refrigerating plant.
The present invention is mainly used in the ammonia-water absorption-type refrigeration device that utilizes using waste heat from tail gas on the fishing boat, and in addition, it also is applicable in the refrigerating plant that similarly utilizes engine tail gas waste-heat.
Description of drawings
Fig. 1 is the structure schematic flow sheet of tail gas heat exchanger of the used in ammonia water absorption refrigeration device that utilizes using waste heat from tail gas of one embodiment of the invention.
The specific embodiment
By following embodiment the present invention is further elaborated.
A kind of ammonia-water absorption-type refrigeration device that utilizes using waste heat from tail gas, as shown in Figure 1, comprise waste heat generator 1, carry and heat up in a steamer device 2, regenerator 3, rectifier 4, generation-absorption heat exchanger 5, absorber 6, solution pump 7, condenser 8, return cooler 9, solution choke valve 10, choke valve 11, second throttle valve 12, an evaporimeter 13, send cold terminal 14 (being external in the circulatory system), connect and constitute the closed circuit of ammonia spirit and the closed circuit of ammonia respectively by pipeline.Wherein waste heat generator 1 is a tube shell type structure, ammonia spirit is walked tube side, the tube side taphole of waste heat generator 1 is connected with the input of regenerator 3, the vapour-liquid of its tube side is imported and exported and is carried the bottom of heating up in a steamer the device 2 and the assembly of regenerator 3 and be connected, and waste heat generator 1 is in the closed circuit of the closed circuit of ammonia spirit and ammonia simultaneously.
Outside the integral body of described ammonia absorption type refrigerating plant, also be circumscribed with tail gas heat exchanger 15 and vapour liquid separator 16.Tail gas heat exchanger 15 is a kind of steam generators, adopt tube shell type structure, its shell side bottom is connected with vapour liquid separator 16 bottoms by liquid back pipe 17, the top of vapour liquid separator 16 is connected with the shell side top of the waste heat generator 1 of described refrigerating plant, and waste heat generator 1 shell side bottom is connected with the liquid back pipe 17 of vapour liquid separator 16 bottoms.Make tube side leave with rage when engines tail and enter tail gas heat exchanger 15 when carrying out heat exchange, tail gas heat exchanger 15 just can make working medium produce moist steam, and (working medium is water in the present embodiment, what produce is water vapour) walk shell side and enter vapour liquid separator 16, isolated steam enters the top of waste heat generator 1 shell side from the top of vapour liquid separator 16, to in waste heat generator 1, walking the ammonia spirit heating of tube side, make the refrigerating plant system carry out the circulation of ammonia spirit and the circulation of ammonia.Meanwhile, steam is condensed into liquid after the heat exchange in waste heat generator 1, because the setting height(from bottom) of tail gas heat exchanger 15 and vapour liquid separator 16 is lower than waste heat generator 1, condensed liquid is under the gravity effect of difference in height, turn back to the liquid back pipe 17 of vapour liquid separator 16 bottoms from waste heat generator 1 shell side bottom, get back to the shell side bottom of tail gas heat exchanger 15 again from this liquid back pipe 17.In addition, separate the remaining liquid in back from vapour liquid separator 16 in the early time and also turn back to tail gas heat exchanger 15 through liquid back pipe 17 from vapour liquid separator 16 bottoms.This two-part liquid is heated by tail gas again in tail gas heat exchanger 15, so circulation, thereby the utilizing waste heat for refrigeration process of realization ammonia absorption type refrigerating plant.The tail gas heat exchanger 15 of tube shell type structure all is carved with thread groove on every tubulation tube wall in its tubulation family, to strengthen the heat exchange effect.
Claims (4)
1, a kind of tail gas heat exchanger of utilizing the used in ammonia water absorption refrigeration device of using waste heat from tail gas, comprise the waste heat generator that is installed in the described ammonia-water absorption-type refrigeration device, it is characterized in that: the shell side vapour-liquid at described waste heat generator is imported and exported the tail gas heat exchanger that is connected to peripheral hardware.
2, the tail gas heat exchanger of utilizing the used in ammonia water absorption refrigeration device of using waste heat from tail gas according to claim 1, it is characterized in that: described tail gas heat exchanger is a steam generator, adopt tube shell type structure, tail gas is walked tube side, steam is walked shell side, between tail gas heat exchanger and waste heat generator, also be provided with vapour liquid separator, tail gas heat exchanger shell side top is connected with the steam inlet of vapour liquid separator, tail gas heat exchanger shell side bottom is connected by liquid back pipe with the vapour liquid separator bottom, the top of vapour liquid separator is connected with waste heat generator shell side top, and waste heat generator shell side bottom is connected with liquid back pipe.
3, the tail gas heat exchanger of utilizing the used in ammonia water absorption refrigeration device of using waste heat from tail gas according to claim 1 and 2 is characterized in that: in the row tube bundle in the described tail gas heat exchanger, all be carved with thread groove on the every tubulation tube wall.
4, the tail gas heat exchanger of utilizing the used in ammonia water absorption refrigeration device of using waste heat from tail gas according to claim 1 and 2 is characterized in that: the installation site of described tail gas heat exchanger is lower than the waste heat generator in the ammonia-water absorption-type refrigeration device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2007100269944A CN100453927C (en) | 2007-02-12 | 2007-02-12 | Exhaust gas heat exchanger used in ammonia water absorption refrigeration device using residual heat of exhaust gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2007100269944A CN100453927C (en) | 2007-02-12 | 2007-02-12 | Exhaust gas heat exchanger used in ammonia water absorption refrigeration device using residual heat of exhaust gas |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101017040A true CN101017040A (en) | 2007-08-15 |
| CN100453927C CN100453927C (en) | 2009-01-21 |
Family
ID=38726201
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2007100269944A Expired - Fee Related CN100453927C (en) | 2007-02-12 | 2007-02-12 | Exhaust gas heat exchanger used in ammonia water absorption refrigeration device using residual heat of exhaust gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100453927C (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102428327A (en) * | 2009-05-08 | 2012-04-25 | 山石科技有限公司 | Gas-fired heat pump water heater |
| CN113899110A (en) * | 2021-11-15 | 2022-01-07 | 中国科学院理化技术研究所 | Absorption type cooling and heating combined supply system with intermediate process |
| CN114234471A (en) * | 2021-11-29 | 2022-03-25 | 中国科学院理化技术研究所 | Absorption type combined cooling and heating system |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4079576B2 (en) * | 2000-06-05 | 2008-04-23 | 三洋電機株式会社 | Absorption refrigerator |
| JP2002295924A (en) * | 2001-03-29 | 2002-10-09 | Takuma Co Ltd | Ammonia absorption freezer |
| US6694772B2 (en) * | 2001-08-09 | 2004-02-24 | Ebara Corporation | Absorption chiller-heater and generator for use in such absorption chiller-heater |
| JP2003222434A (en) * | 2002-01-30 | 2003-08-08 | Ebara Corp | Regenerator for exhaust gas drive absorption water heater-chiller |
| CN1233990C (en) * | 2003-11-18 | 2005-12-28 | 华中科技大学 | Detection equipment of Coriolis mass flow meter |
| CN201014846Y (en) * | 2007-02-12 | 2008-01-30 | 庞启东 | Tail gas heat exchanger for ammonia water absorption refrigerator using after heat of tail gas |
-
2007
- 2007-02-12 CN CNB2007100269944A patent/CN100453927C/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102428327A (en) * | 2009-05-08 | 2012-04-25 | 山石科技有限公司 | Gas-fired heat pump water heater |
| CN113899110A (en) * | 2021-11-15 | 2022-01-07 | 中国科学院理化技术研究所 | Absorption type cooling and heating combined supply system with intermediate process |
| CN114234471A (en) * | 2021-11-29 | 2022-03-25 | 中国科学院理化技术研究所 | Absorption type combined cooling and heating system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100453927C (en) | 2009-01-21 |
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| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Free format text: FORMER OWNER: ZHANG WENHUI Owner name: FOSHAN HUIKONG HEAT ENERGY REFRIGERATION TECHNOLOG Free format text: FORMER OWNER: PANG QIDONG Effective date: 20101207 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 528000 FOSHAN SOUTHEAST ELECTRICAL APPLIANCE CO., LTD., NO.29, JIANGWAN ROAD 1, CHANCHENG DISTRICT, FOSHAN CITY, GUANGDONG PROVINCE TO: 528000 ROOM 1703, TOWER A, NO.68, TONGJI ROAD, CHANCHENG DISTRICT, FOSHAN CITY, GUANGDONG PROVINCE |
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| TR01 | Transfer of patent right |
Effective date of registration: 20101207 Address after: 528000, room 1703, block A, Tongji Road, Chancheng District, Guangdong, Foshan, 68 Patentee after: Foshan Huikong Heat Energy RefrigerationTechnology Co., Ltd. Address before: 528000, Guangdong, Chancheng, Jiangwan Foshan Road, No. 29 Foshan southeast Electrical Appliance Co., Ltd. Co-patentee before: Zhang Wenhui Patentee before: Pang Qidong |
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| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090121 Termination date: 20190212 |