CN201014837Y - Supercritical refrigeration energy-saving device for lithium bromide absorption refrigerating machine - Google Patents

Supercritical refrigeration energy-saving device for lithium bromide absorption refrigerating machine Download PDF

Info

Publication number
CN201014837Y
CN201014837Y CNU2007200196169U CN200720019616U CN201014837Y CN 201014837 Y CN201014837 Y CN 201014837Y CN U2007200196169 U CNU2007200196169 U CN U2007200196169U CN 200720019616 U CN200720019616 U CN 200720019616U CN 201014837 Y CN201014837 Y CN 201014837Y
Authority
CN
China
Prior art keywords
water
unit
cooling
lithium
low temperature
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.)
Expired - Fee Related
Application number
CNU2007200196169U
Other languages
Chinese (zh)
Inventor
王长迎
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JINAN KEXING AIR CONDITIONER CO Ltd
Original Assignee
JINAN KEXING AIR CONDITIONER CO Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by JINAN KEXING AIR CONDITIONER CO Ltd filed Critical JINAN KEXING AIR CONDITIONER CO Ltd
Priority to CNU2007200196169U priority Critical patent/CN201014837Y/en
Application granted granted Critical
Publication of CN201014837Y publication Critical patent/CN201014837Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P80/00Climate change mitigation technologies for sector-wide applications
    • Y02P80/10Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier

Abstract

An energy-saving device for supercritical cooling of lithium-bromide absorption refrigerating machines, which essentially provides a means of energy-saving, comprising a condenser and cryogenerator unit and an evaporator and absorber unit, as well as a cooling water cycling pipeline that passes the condenser and cryogenerator unit and the evaporator and absorber unit, characterized in that: the cooling water of the cooling water cycling pipeline is low-temperature underground water. Neither the manufacturing nor the application of the utility model produces contaminants, thus the utility model is environment-friendly, energy-saving and water-saving; besides, the utility model can reduce the emission of greenhouse gases and greatly cut the manufacture and running cost, and can be widely applied to hotels, guesthouses, chemical engineering, smelting, foods processing and medication etc.

Description

A kind of lithium bromide absorption type refrigerator super critical cooling and energy conserving device
Technical field
The utility model relates to lithium-bromide absorption-type refrigerating machine condensation, absorber cooling water cycle art, is a kind of lithium bromide absorption type refrigerator super critical energy saver specifically.
Background technology
Lithium bromide refrigerator originates from U.S. forties in 20th century, is succeeded in developing by doctor Kai Li, and promotes the use of in the whole world.The sixties in 20th century, 704 first the lithium bromide units in China Shanghai are trial-produceed successfully, because the energy-conservation advantage of its uniqueness, use to 21 century in China's large-scale popularization to the initial stage eighties, along with the input of continuous progress in science and technology and scientific research fund, the lithium-bromide absorption-type refrigerating machine power-saving technology has obtained the changes and improvements of making rapid progress.
Though through research and the improvement of decades, still there is a lot of defectives in lithium-bromide absorption-type refrigerating machine aspect energy-conservation, make the lithium-bromide absorption-type refrigerating machine of producing now, the operation of condensation, absorber has dual mode usually:
1, series connection: cooling water is introduced into absorber cooling lithium-bromide solution; Enter condenser condenses high and low temperature refrigerant vapour again, enter cooling tower cooling cool cycles then and use;
2, parallel connection: cooling water enters absorption, condenser simultaneously, enters cooling tower cooling cool cycles then and uses.
These two kinds of methods of operation have directly increased the production and the operating cost of lithium-bromide absorption-type refrigerating machine.Because the inlet temperature of these two kinds of method of operation cooling waters is that 32 ℃, outlet temperature are 37.5 ℃.During the lithium-bromide absorption-type refrigerating machine operation; the out temperature of cooling water is high more; coolant water temperature especially for cooler condenser is high more; consumption to the energy and cooling water is big more, directly causes a large amount of consumption of the energy and water, and refrigerating efficiency reduces; greenhouse gas emissions increase; the circulation that goes round and begins again causes the waste of the energy and water resource, is unfavorable for protecting environment and energy savings.
The utility model content
In order to remedy above-mentioned the deficiencies in the prior art; the utility model provides a kind of lithium bromide absorption type refrigerator super critical cooling and energy conserving device; the lithium-bromide absorption-type refrigerating machine condensation of this device, absorber sub-cooled circularly cooling mode with energy savings and water resource, help protecting environment.
The technical solution of the utility model is: this kind lithium bromide absorption type refrigerator super critical cooling and energy conserving device, comprise condensation, cryogenerator unit and evaporation, absorber unit, the cooling water circulation line is by described condensation, cryogenerator unit and evaporation, absorber unit, it is characterized in that the cooling water of described cooling water circulation line uses low temperature underground water.
The further technical scheme of the utility model is:
For the type of cooling, a kind of scheme is: the low temperature underground water that flows into condensation, cryogenerator unit and evaporation, absorber unit is a circulation line.Another kind of scheme is: low temperature underground water flows into condensation, cryogenerator unit and evaporation, absorber unit respectively by corresponding circulation line.
16-18 ℃ of this underground water water temperature is made up of two low temperature deep wells, a glance water intaking, and a glance nature or pressurization are recharged.Also can use many low temperature deep wells.
The beneficial effects of the utility model are:
Use low temperature underground water to enter condenser, by changing (reduction) condensation temperature and pressure, rapidly the lithium-bromide solution heating is concentrated, the high and low temperature refrigerant vapour of generation is condensed into cryogenic coolant water, enters the evaporator evaporation refrigeration.Use low temperature underground water to enter absorber and cool off dense lithium-bromide solution, by reducing the dense lithium-bromide solution temperature of absorber, change (reduction) evaporating temperature and pressure, improve the operating efficiency of absorber, allow the refrigerant vapour of dense lithium-bromide solution fast Absorption evaporator evaporation under the cryogenic vacuum environment, increase refrigerating capacity; Reduce and make and operating cost, reduce the consumption of the energy and water resource.Inject underground cooling after the low temperature underground water of condensation, absorber heats up, recycle, reduce greenhouse gas emission, the conservation of nature environment.
Its principle is as follows:
Refrigeration needs to consume a large amount of energy, water vapour condensation at normal temperatures usually, and cooling water 32-37.5 ℃, flow one timing of refrigerating capacity and cooling water, the consumption of the energy remains unchanged, and the consumption of cooling water and greenhouse gas emission increase.
If create a lower environment temperature, under vacuum state, allow heated medium heat up rapidly, water at low temperature is cooled off the water vapour condensation rapidly, allow lithium-bromide solution absorb the refrigerant vapour refrigeration of evaporimeter rapidly, the consumption of the energy and water resource and the discharge capacity of greenhouse gases will be reduced significantly.
Lithium-bromide solution is under vacuum state, and with the heating of the lithium-bromide solution in the high-temperature generator, lithium-bromide solution concentrates through heating with natural gas, steam or other energy, produces the high temperature refrigerant vapour; The high temperature refrigerant vapour heats the lithium-bromide solution of cryogenerator again, and the lithium-bromide solution of cryogenerator concentrates through heating, produces cryogenic coolant steam.
Underground low temperature water enters condenser, changed (reductions) condensation temperature and pressure, and the interior refrigerant vapour of high and low temperature generator cools off through condenser, is condensed into water as refrigerant rapidly.
Underground low temperature underground water enters absorber, cools off dense lithium-bromide solution, and fast Absorption steam has changed (reductions) temperature and pressure of evaporimeter has improved absorption efficiency, the refrigerating capacity increase.
The refrigerant vapor in the high cryogenerator of cryogenically having descended water condensation has absorbed the heat of evaporator evaporation and has heated up, and the low temperature underground water after the intensification injects underground cooling through inverted well and recycles.
The lithium-bromide absorption-type refrigerating machine of the utility model production can be widely used in industries such as hotel, hotel, chemical industry, smelting, food, medicine.Production of the present utility model and using method do not have any pollutant emission, help protecting environment, and energy savings and water resource reduce greenhouse gas emission, reduce significantly and make and operating cost.
Description of drawings
Figure is a fundamental diagram of the present utility model.
The specific embodiment
As figure.This kind lithium bromide absorption type refrigerator super critical cooling and energy conserving device comprises condensation, cryogenerator unit and evaporation, absorber unit, and the cooling water circulation line is by described condensation, cryogenerator unit and evaporation, absorber unit; Also comprise high-temperature generator, solution heat exchanger, solution circulation pump and switch board etc.Its connected mode and the course of work are same as the prior art.
Its improvements are that the cooling water inlet of cooling water circulation line is positioned at condensation, cryogenerator unit one end, and coolant outlet is positioned at evaporation, absorber unit one end.Cooling water uses low temperature underground water.16-18 ℃ of this underground water water temperature is made up of two low temperature deep wells, a glance water intaking, and a glance nature or pressurization are recharged.Cooling water also can by with above-mentioned water supply direction recycled back.
Use low temperature underground water to enter condenser, by changing (reduction) condensation temperature and pressure, rapidly the lithium-bromide solution heating is concentrated, the high and low temperature refrigerant vapour of generation is condensed into cryogenic coolant water, enters the evaporator evaporation refrigeration.Use low temperature underground water to enter absorber and cool off dense lithium-bromide solution, by reducing the dense lithium-bromide solution temperature of absorber, change (reduction) evaporating temperature and pressure, improve the operating efficiency of absorber, allow the refrigerant vapour of dense lithium-bromide solution fast Absorption evaporimeter under low temperature environment, increase refrigerating capacity; Reduce and make and operating cost, reduce the consumption of the energy and water resource.Inject underground cooling after the low temperature underground water of condensation, absorber heats up, recycle, reduce greenhouse gas emission, the conservation of nature environment.
Its groundwork process is:
1), the lithium-bromide solution of natural gas, steam or other energy heating high-temperature generator, after the lithium-bromide solution heating concentrates, produce the high temperature refrigerant vapour;
2), the lithium-bromide solution of high temperature refrigerant vapour heating cryogenerator, after the lithium-bromide solution heating concentrates, produce cryogenic coolant steam;
3), low temperature underground water enters condenser, changes the temperature and pressure of (reductions) condenser, and the rapid condensation of high and low temperature refrigerant vapour (cooling) is become cryogenic coolant water, enters evaporimeter, condensation rate quickening, energy resource consumption reduction;
4), low temperature underground water enters absorber and cools off dense lithium-bromide solution, change (reduction) evaporating temperature and pressure, dense lithium-bromide solution is the refrigerant vapour refrigeration of fast Absorption evaporator evaporation at low temperatures, and the absorption efficiency of absorber improves, and the refrigerating capacity of evaporimeter increases;
5), after the low temperature underground water of condensation, absorber heats up, inject underground cooling, recycle through inverted well.
6), condensed high and low temperature refrigerant vapour condensate water enters evaporator evaporation through the condenser throttle pipe, absorbed the heat of evaporimeter by the absorber concentrated solution;
7), bromize lithium concentrated solution is through cooling, absorbed the heat of evaporimeter after, become weak solution, weak solution through the heat exchange of high and low temperature heat exchanger, is sent to the circulation of high and low temperature generator by generating pump.
In step (1), (2), (3), (4), (5), following (comparing with original equipment) distinguished in each technological parameter operation: step (1), (2) energy resource consumption reduce about 30%; Step (1), (4) greenhouse gas emission reduce about 30%; Step (3) condenser condenses temperature is approximately less than 30 ℃, and condensing pressure is less than 40 millimetress of mercury, and cooling water flow reduces 40% approximately; Step (4) evaporator evaporation pressure is less than 6 millimetress of mercury, and evaporating temperature is less than 4 ℃; Step (5) low temperature underground water injects underground recycling, and water consumption is zero substantially; Greenhouse gas emission is reclaimed the discord atmosphere by soil and is directly contacted.Above-mentioned data show that the lithium-bromide absorption-type refrigerating machine evaporating temperature working near under the critical condition.
The technical solution of the utility model is not limited to so.For example:
For the type of cooling, can also adopt another kind of scheme: low temperature underground water flows into condensation, cryogenerator unit and evaporation, absorber unit respectively by corresponding circulation line.
The low temperature deep well also can use many.

Claims (4)

1. lithium bromide absorption type refrigerator super critical cooling and energy conserving device, comprise condensation, cryogenerator unit and evaporation, absorber unit, the cooling water circulation line is by described condensation, cryogenerator unit and evaporation, absorber unit, it is characterized in that the cooling water of described cooling water circulation line uses low temperature underground water.
2. a kind of lithium bromide absorption type refrigerator super critical cooling and energy conserving device according to claim 1 is characterized in that, the low temperature underground water that flows into condensation, cryogenerator unit and evaporation, absorber unit is a circulation line.
3. a kind of lithium bromide absorption type refrigerator super critical cooling and energy conserving device according to claim 1 is characterized in that, low temperature underground water flows into condensation, cryogenerator unit and evaporation, absorber unit respectively by corresponding circulation line.
4. according to claim 1 or 2 or 3 described a kind of lithium bromide absorption type refrigerator super critical cooling and energy conserving devices, it is characterized in that 16-18 ℃ of underground water water temperature is made up of two low temperature deep wells, a glance water intaking, a glance nature or pressurization are recharged.
CNU2007200196169U 2007-03-19 2007-03-19 Supercritical refrigeration energy-saving device for lithium bromide absorption refrigerating machine Expired - Fee Related CN201014837Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2007200196169U CN201014837Y (en) 2007-03-19 2007-03-19 Supercritical refrigeration energy-saving device for lithium bromide absorption refrigerating machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2007200196169U CN201014837Y (en) 2007-03-19 2007-03-19 Supercritical refrigeration energy-saving device for lithium bromide absorption refrigerating machine

Publications (1)

Publication Number Publication Date
CN201014837Y true CN201014837Y (en) 2008-01-30

Family

ID=39026635

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2007200196169U Expired - Fee Related CN201014837Y (en) 2007-03-19 2007-03-19 Supercritical refrigeration energy-saving device for lithium bromide absorption refrigerating machine

Country Status (1)

Country Link
CN (1) CN201014837Y (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104329760A (en) * 2014-11-13 2015-02-04 中冶北方(大连)工程技术有限公司 System and method for comprehensive utilization of ground heat of mine water drainage
CN109990502A (en) * 2019-04-16 2019-07-09 廊坊新奥泛能网络科技服务有限公司 Distributed energy resource system and its for cooling method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104329760A (en) * 2014-11-13 2015-02-04 中冶北方(大连)工程技术有限公司 System and method for comprehensive utilization of ground heat of mine water drainage
CN109990502A (en) * 2019-04-16 2019-07-09 廊坊新奥泛能网络科技服务有限公司 Distributed energy resource system and its for cooling method

Similar Documents

Publication Publication Date Title
CN100501272C (en) System and method for transforming low temperature residual heat into steam
CN103411347B (en) Coupling type heat pump waste heat recovery system
CN103629854A (en) Ammonia and lithium bromide integrated absorption refrigeration device driven by heating medium water and method
CN103808060B (en) Band flash vessel two-stage absorbs Equations of The Second Kind lithium bromide absorption type heat pump unit
CN107490210A (en) The absorption waste heat recovery type heat pump circulatory system of compression and its method of thermal coupling
CN203704433U (en) Two-stage lithium bromide absorption heat transformer unit with flash evaporator
CN105066508B (en) A kind of efficient injection absorption refrigerating machine for freezing and refrigeration
CN201014837Y (en) Supercritical refrigeration energy-saving device for lithium bromide absorption refrigerating machine
CN104101131A (en) Absorption refrigerator for refrigerating and heating by using recovered heat energy and refrigerating and heating method thereof
CN202914146U (en) Improved vacuum exhaust heat pump type steam turbine generating system
CN105066502B (en) A kind of direct-fired absorption refrigeration method and device for reclaiming the heat of transformation
CN105115184B (en) A kind of absorbent refrigeration system with cryogenic refrigeration function
CN207741379U (en) A kind of absorption deep refrigerating system of industrial waste heat driving
CN207585140U (en) One kind is based on the second kind absorption type mixing heat pump
CN103808059B (en) Secondary generation secondary absorbs Equations of The Second Kind lithium bromide absorption type heat pump unit
CN201844611U (en) Energy-saving deep refrigeration device
CN104651004A (en) Energy-saving coal-based natural gas process
CN101021371A (en) Lithium bromide absorption type refrigerator super critical cooling and energy conserving device
CN203704432U (en) Secondary-generating and secondary-absorbing second type lithium bromide absorption type heat pump unit
CN211233436U (en) Two-section lithium bromide absorption heat pump unit capable of achieving double-effect refrigeration
CN203572091U (en) Heating-medium-water-driving ammonia and lithium bromide integrated absorption refrigeration device
CN211177494U (en) Single-effect heating and double-effect refrigerating two-section type lithium bromide absorption heat pump unit
CN108507219A (en) A kind of compound two-stage type lithium bromide absorption type heat pump and working method
CN211233437U (en) Single-effect heating and double-effect refrigerating steam type lithium bromide absorption heat pump unit
CN201028878Y (en) Energy-saving device of lithium bromide absorption type refrigerator for producing sanitary hot water when refrigeration

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20080130

Termination date: 20100319