CN208154866U - System for heating by utilizing waste heat of high-temperature coal tar distillation warm water system - Google Patents

System for heating by utilizing waste heat of high-temperature coal tar distillation warm water system Download PDF

Info

Publication number
CN208154866U
CN208154866U CN201820636662.1U CN201820636662U CN208154866U CN 208154866 U CN208154866 U CN 208154866U CN 201820636662 U CN201820636662 U CN 201820636662U CN 208154866 U CN208154866 U CN 208154866U
Authority
CN
China
Prior art keywords
warm water
heat exchanger
water
circulating
heating
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
CN201820636662.1U
Other languages
Chinese (zh)
Inventor
何宗保
张树福
何文伟
单春华
叶煌
高栋
周志春
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.)
Acre Coking and Refractory Engineering Consulting Corp MCC
Original Assignee
Acre Coking and Refractory Engineering Consulting Corp MCC
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 Acre Coking and Refractory Engineering Consulting Corp MCC filed Critical Acre Coking and Refractory Engineering Consulting Corp MCC
Priority to CN201820636662.1U priority Critical patent/CN208154866U/en
Application granted granted Critical
Publication of CN208154866U publication Critical patent/CN208154866U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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]
    • Y02B30/12—Hot water central heating systems using heat pumps
    • 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

  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

The utility model relates to a system for heating by utilizing waste heat of a high-temperature coal tar distillation warm water system, which comprises a circulating warm water system, a circulating water system, a warm water-circulating water heat exchanger, a lithium bromide absorption heat pump unit and a standing power station; the circulating warm water system consists of a warm water pipeline, a warm water branch pipeline, a naphthalene oil-warm water heat exchanger, a wash oil-warm water heat exchanger, an anthracene oil-warm water heat exchanger, a distillation tower top reflux-warm water heat exchanger and a warm water circulating pump; the utility model discloses utilize lithium bromide absorption heat pump unit to high temperature coal tar distillation warm water system's waste heat recovery for the heating and the life hot water of office building, each building factory building, the mode that the alternative energy consumption carries out the heating can effectively reduce the production energy consumption, improves the utilization efficiency of the energy, reduces user's cost.

Description

Utilize the system of high temperature coal-tar distillation Water heating system waste heating
Technical field
The utility model relates to coal tar distillation and technical field of waste heat utilization more particularly to it is a kind of utilize high temperature coal-tar Distill the system of Water heating system waste heating.
Background technique
Coal tar distillation is one of key step of coal tar processing.Coal tar distillation is will by tar heating furnace Coal tar is heated to very high temperature, and then different parts produce out the process for evaporating a little different products in destilling tower.
Currently, the product of side take-off mainly has naphtalene oil, washing oil, a carbolineum, anthracene oil etc. after high temperature coal-tar distillation, this A little side take-off products are to exchange heat to condense first with raw material coal tar, then be cooled to suitable temperature with warm water.Using warm water Cooling is to be not suitable for using lower temperature because these side take-off products all have the characteristics that low temperature easily crystallizes, easily blocks pipeline Recirculated water cool down, the temperature of cooling warm water is generally at 60-65 DEG C.Warm water after having cooled down side take-off product passes through temperature Water-Heat Exchanger in Circulating Water System takes heat away with the recirculated water of lower temperature, and temperature is again lowered to 60-65 DEG C of realization circulation benefit With.With this partial heat of circulation water coke slurry, accounting is very big compared with distilling heat consumption, is all finally by running between recirculated water It puts into atmosphere, causes energy waste.I.e. the heat of warm water does not recycle sufficiently, increases the water of energy consumption and recirculated water Consumption, reduces capacity usage ratio.
At the same time, the office building in production area, each factory building heating and domestic hot-water need a large amount of heating again Water.The heat of usual heating water is provided by steam boiler or hot-water boiler, is needed to consume fuel combustion and is converted to heat, both Energy is wasted, and increases investment.
Summary of the invention
The utility model provides a kind of system using high temperature coal-tar distillation Water heating system waste heating, utilizes bromination Lithium-absorbing formula heat pump unit adopts the Waste Heat Recovery of high temperature coal-tar distillation Water heating system for office building, each factory building Warm and domestic hot-water, the substitution consumption energy carry out the mode of heating, can effectively reduce production energy consumption, and that improves the energy utilizes effect Rate reduces the cost of user.
In order to achieve the above object, the utility model is implemented with the following technical solutions：
Using high temperature coal-tar distillation Water heating system waste heating system, including circulation Water heating system, circulation, Warm water-Heat Exchanger in Circulating Water System, lithium bromide absorption type heat pump unit and thermal substation；The circulation Water heating system is by warm water pipe, temperature Moisture branch pipe(tube), naphtalene oil-warm water heat exchanger, washing oil-warm water heat exchanger, one carbolineum-warm water heat exchanger, anthracene oil-warm water heat exchange Device, overhead reflux-warm water heat exchanger and Warm water circulation pump group at, 5 warm water laterals are parallel on warm water pipe, Naphtalene oil-warm water heat exchanger, washing oil-warm water heat exchanger, one carbolineum-warm water heat exchanger, two anthracenes are set on 5 warm water laterals respectively Oil-warm water heat exchanger and overhead reflux-warm water heat exchanger；Warm water circulation pump and warm water-recirculated water are set on warm water pipe Heat exchanger；Lithium bromide absorption type heat pump unit includes evaporator, absorber, generator and condenser；Warm water-Heat Exchanger in Circulating Water System It is connected by circulating water pipeline with circulation；Warm water-Heat Exchanger in Circulating Water System upstream warm water pipe and generator inlet and Evaporator inlet is connected, and warm water-Heat Exchanger in Circulating Water System downstream warm water pipe is connected with generator exports and evaporator outlet, cold Condenser entrance and condensator outlet pass through circulating water pipeline respectively and are connected with circulation；Absorber outlet and the one of thermal substation Grade heat supply network water supply line is connected, and absorber entrance is connected with the first-degree heating network water return pipeline of thermal substation, the first-degree heating network of thermal substation Heating water-circulating pump is set on water return pipeline；In addition thermal substation connects user heating water water supply line and user heating water return pipe Road.
The Warm water circulation pump is set to warm water-Heat Exchanger in Circulating Water System upstream, and Warm water circulation pumps on the warm water pipe of upstream If supplementing warm water entrance, supplement warm water entrance is connected with the warm water export of warm water tank；Steam inlet and pot are additionally provided on warm water tank Furnace water inlet.
On the warm water pipe in warm water-Heat Exchanger in Circulating Water System upstream and downstream, generator inlet and evaporator inlet upstream Warm water pipe on, on the warm water pipe in generator exports and evaporator outlet downstream set valve respectively；Warm water-recirculated water heat exchange Manually-operated gate is set on circulating water pipeline before device.
Compared with prior art, the utility model has the beneficial effects that：
Using lithium bromide absorption type heat pump unit the Waste Heat Recovery of high temperature coal-tar distillation Water heating system, for handling official business Building, the heating of each factory building and domestic hot-water, the substitution consumption energy carry out the mode of heating, can effectively reduce production energy consumption, The utilization efficiency for improving the energy, reduces the cost of user.
Detailed description of the invention
Fig. 1 is the structural representation of the system described in the utility model using high temperature coal-tar distillation Water heating system waste heating Figure.
In figure：1. recycling 11. warm water pipe of Water heating system, 12. 13. naphtalene oils of warm water lateral-warm water heat exchanger 14. washing oil -15. 1 carbolineums of warm water heat exchanger -16. anthracene oils of warm water heat exchanger-warm water heat exchanger, 17. overhead returns 18. Warm water circulation of stream-warm water heat exchanger pumps 19. 2. warm water of warm water tank-Heat Exchanger in Circulating Water System, 31. recirculated water inlet duct 32. 4. lithium bromide absorption type heat pump unit of circulating water outlet pipeline, 41. evaporator inlet, 42. evaporator outlet 43. absorbs 44. absorber of device entrance exports 45. condenser inlet, 46. condensator outlet, 47. generator inlet, 48. generator exports 54. user heating of water-circulating pump 5. 51. first-degree heating network water supply line of thermal substation, 52. first-degree heating network water return pipeline 53. heats 55. 6. valve of user heating water water return pipeline of water water supply line, 7. manually-operated gate
Specific embodiment
Specific embodiment of the present utility model is described further with reference to the accompanying drawing：
As shown in Figure 1, the system described in the utility model using high temperature coal-tar distillation Water heating system waste heating, including Recycle Water heating system 1, circulation, warm water-Heat Exchanger in Circulating Water System 2, lithium bromide absorption type heat pump unit 4 and thermal substation 5；Institute Circulation Water heating system 1 is stated by warm water pipe 11, warm water lateral 12, naphtalene oil-warm water heat exchanger 13, washing oil-warm water heat exchanger 14, one carbolineum-warm water heat exchanger 15, anthracene oil-warm water heat exchanger 16, overhead reflux-warm water heat exchanger 17 and warm water Circulating pump 18 forms, and is parallel on 5 warm water laterals, 12,5 warm water laterals 12 on warm water pipe 11 and sets naphthalene respectively Oil-warm water heat exchanger 13, washing oil-warm water heat exchanger 14, one carbolineum-warm water heat exchanger 15, anthracene oil-warm water heat exchanger 16 and steaming Evaporate column overhead reflux-warm water heat exchanger 17；Warm water circulation pump 18 and warm water-Heat Exchanger in Circulating Water System 2 are set on warm water pipe 11；Bromination Lithium-absorbing formula heat pump unit 4 includes evaporator, absorber, generator and condenser；Warm water-Heat Exchanger in Circulating Water System 2 passes through circulation Waterpipe 3 is connected with circulation；The warm water pipe 11 and generator inlet 47 of 2 upstream of warm water-Heat Exchanger in Circulating Water System and steaming It sends out device entrance 41 to be connected, the warm water pipe 11 and generator exports 48 and evaporator outlet 42 in 2 downstream of warm water-Heat Exchanger in Circulating Water System It is connected, condenser inlet 45 and condensator outlet 46 are connected by circulating water pipeline 3 with circulation respectively；Absorber outlet 44 are connected with the first-degree heating network water supply line 51 of thermal substation 5, the first-degree heating network water return pipeline 52 of absorber entrance 43 and thermal substation 5 It is connected, heating water-circulating pump 53 is set on the first-degree heating network water return pipeline 52 of thermal substation 5；In addition thermal substation 5 connects user heating water Water supply line 54 and user heating water water return pipeline 55.
The Warm water circulation pump 18 is set to the upstream of warm water-Heat Exchanger in Circulating Water System 2, and Warm water circulation pumps the warm water tube of 18 upstreams Supplement warm water entrance is set on road 11, supplement warm water entrance is connected with the warm water export of warm water tank 19；Steaming is additionally provided on warm water tank 19 Vapour entrance and boiler water inlet.
On the warm water pipe 11 in 2 upstream of warm water-Heat Exchanger in Circulating Water System and downstream, generator inlet 47 and evaporator inlet Valve 6 is set respectively on the warm water pipe 11 of 41 upstreams, on the warm water pipe 11 in 42 downstream of generator exports 48 and evaporator outlet； Manually-operated gate 7 is set on circulating water pipeline 11 before warm water-Heat Exchanger in Circulating Water System 2.
Working method described in the utility model using high temperature coal-tar distillation Water heating system waste heating system is as follows：
1) it in high temperature coal-tar distillation Water heating system, by tar heating furnace by tar heating, is then adopted in destilling tower side line A little different products, including naphtalene oil, washing oil, a carbolineum, anthracene oil are evaporated out；These side take-off products first respectively with raw material coal tar Oil heat exchange condensation, then exchange heat with circulation Water heating system 1；In circulation Water heating system 1, with 60~65 DEG C of warm water to side take-off Product is cooled down, and the temperature of warm water is increased to 75~80 DEG C；Recycle Water heating system 1 again by warm water-Heat Exchanger in Circulating Water System 2 with The temperature of warm water is reduced to after 60~65 DEG C again and is re-used for cooling side take-off product, so follows by circulation heat exchange Ring；In the process, warm water periodically is supplemented into circulation Water heating system 1；
2) waste heat of the recycling circulation Water heating system 1 of lithium bromide absorption type heat pump unit 4 is utilized；Lithium bromide absorption type heat pump machine Group 4 includes evaporator, absorber, generator and condenser；By the warm water pipe 11 of 1 upstream of warm water-Heat Exchanger in Circulating Water System and hair Raw device entrance 47 and evaporator inlet 41 are connected, the warm water pipe 11 and generator exports 48 in 2 downstream of warm water-Heat Exchanger in Circulating Water System And evaporator outlet 42 is connected, condenser inlet 45 and condensator outlet 46 pass through circulating water pipeline 3 and circulation respectively It is connected；Absorber outlet 44 is connected with the first-degree heating network water supply line 51 of thermal substation 5, and the one of absorber entrance 43 and thermal substation 5 Grade heat supply network water return pipeline 52 is connected；By lithium bromide refrigerators heat pump unit 4, the waste heat in warm water is transmitted to thermal substation 5 In first-degree heating network；
3) it by thermal substation 5, heats to user, realizes the abundant benefit of high temperature coal-tar distillation Water heating system waste heat With；
4) on the warm water pipe 11 in 2 upstream of warm water-Heat Exchanger in Circulating Water System and downstream, generator inlet 47 and evaporator enter Valve is set respectively on the warm water pipe 11 of 41 upstreams of mouth, on the warm water pipe 11 in 42 downstream of generator exports 48 and evaporator outlet 6, it realizes the switching of heating with non-heating state, does not influence coke using the system of high temperature coal-tar distillation Water heating system waste heating The normal operation of oily distillation technique system.
System described in the utility model using high temperature coal-tar distillation Water heating system waste heating, utilizes lithium bromide absorption Formula heat pump unit 4 high temperature coal-tar distillation Water heating system Waste Heat Recovery, and for for office building, each factory building heating and Domestic hot-water realizes the purpose of energy-saving and emission-reduction, especially suitable for in, the high temperature coal-tar distillation technique system of large-scale It matches.
The preferable specific embodiment of the above, only the utility model, but the protection scope of the utility model is not It is confined to this, anyone skilled in the art is within the technical scope disclosed by the utility model, practical according to this Novel technical solution and its utility model design are subject to equivalent substitution or change, should all cover the protection model in the utility model Within enclosing.

Claims (3)

1.利用高温煤焦油蒸馏温水系统废热供暖的系统，其特征在于，包括循环温水系统、循环水系统、温水-循环水换热器、溴化锂吸收式热泵机组及热力站；所述循环温水系统由温水管道、温水分支管道、萘油-温水换热器、洗油-温水换热器、一蒽油-温水换热器、二蒽油-温水换热器、蒸馏塔塔顶回流-温水换热器及温水循环泵组成，温水管道上并联有5个温水分支管道，5个温水分支管道上分别设萘油-温水换热器、洗油-温水换热器、一蒽油-温水换热器、二蒽油-温水换热器及蒸馏塔塔顶回流-温水换热器；温水管道上设温水循环泵及温水-循环水换热器；溴化锂吸收式热泵机组包括蒸发器、吸收器、发生器和冷凝器；温水-循环水换热器通过循环水管道与循环水系统相连；温水-循环水换热器上游的温水管道与发生器入口及蒸发器入口相连，温水-循环水换热器下游的温水管道与发生器出口及蒸发器出口相连，冷凝器入口及冷凝器出口分别通过循环水管道与循环水系统相连；吸收器出口与热力站的一级热网供水管道相连，吸收器入口与热力站的一级热网回水管道相连，热力站的一级热网回水管道上设供暖水循环泵；热力站另外连接用户采暖水供水管道和用户采暖水回水管道。1. A system for heating with waste heat from a high-temperature coal tar distillation warm water system, characterized in that it includes a circulating warm water system, a circulating water system, a warm water-circulating water heat exchanger, a lithium bromide absorption heat pump unit and a thermal station; the circulating warm water system consists of Warm water pipeline, warm water branch pipeline, naphthalene oil-warm water heat exchanger, washing oil-warm water heat exchanger, anthracene oil-warm water heat exchanger, dianthracene oil-warm water heat exchanger, distillation tower top reflux-warm water heat exchange There are 5 warm water branch pipes connected in parallel on the warm water pipe, and the 5 warm water branch pipes are respectively equipped with naphthalene oil-warm water heat exchanger, washing oil-warm water heat exchanger, and anthracene oil-warm water heat exchanger , dianthracene oil-warm water heat exchanger and distillation tower top reflux-warm water heat exchanger; warm water circulation pump and warm water-circulating water heat exchanger are installed on the warm water pipeline; lithium bromide absorption heat pump unit includes evaporator, absorber, generator The warm water-circulating water heat exchanger is connected to the circulating water system through the circulating water pipe; the warm water pipe upstream of the warm water-circulating water heat exchanger is connected to the generator inlet and the evaporator inlet, and the warm water-circulating water heat exchanger The downstream warm water pipeline is connected to the outlet of the generator and the outlet of the evaporator, the inlet of the condenser and the outlet of the condenser are respectively connected to the circulating water system through the circulating water pipeline; the outlet of the absorber is connected to the water supply pipeline of the primary heating network of the thermal station, and the inlet It is connected with the first-level heating network return pipe of the thermal station, and the heating water circulation pump is installed on the first-level heating network return pipe of the thermal station; the thermal station is also connected to the user's heating water supply pipe and the user's heating water return pipe. 2.根据权利要求1所述的利用高温煤焦油蒸馏温水系统废热供暖的系统，其特征在于，所述温水循环泵设于温水-循环水换热器的上游，温水循环泵上游的温水管道上设补充温水入口，补充温水入口与温水槽的温水出口相连；温水槽上还设有蒸汽入口及锅炉水入口。2. The system according to claim 1, characterized in that, the warm water circulating pump is located upstream of the warm water-circulating water heat exchanger, and on the warm water pipeline upstream of the warm water circulating pump. A supplementary warm water inlet is provided, and the supplementary warm water inlet is connected with the warm water outlet of the warm water tank; the warm water tank is also provided with a steam inlet and a boiler water inlet. 3.根据权利要求1所述的利用高温煤焦油蒸馏温水系统废热供暖的系统，其特征在于，在温水-循环水换热器上游及下游的温水管道上、发生器入口及蒸发器入口上游的温水管道上、发生器出口及蒸发器出口下游的温水管道上分别设阀门；温水-循环水换热器前的循环水管道上设手动阀门。3. The system for heating by waste heat of high-temperature coal tar distillation warm water system according to claim 1, characterized in that, on the warm water pipeline upstream and downstream of the warm water-circulating water heat exchanger, on the upstream of the generator inlet and the evaporator inlet Valves are respectively set on the warm water pipeline, the warm water pipeline downstream of the generator outlet and the evaporator outlet; manual valves are set on the circulating water pipeline in front of the warm water-circulating water heat exchanger.
CN201820636662.1U 2018-04-28 2018-04-28 System for heating by utilizing waste heat of high-temperature coal tar distillation warm water system Expired - Fee Related CN208154866U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820636662.1U CN208154866U (en) 2018-04-28 2018-04-28 System for heating by utilizing waste heat of high-temperature coal tar distillation warm water system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820636662.1U CN208154866U (en) 2018-04-28 2018-04-28 System for heating by utilizing waste heat of high-temperature coal tar distillation warm water system

Publications (1)

Publication Number Publication Date
CN208154866U true CN208154866U (en) 2018-11-27

Family

ID=64377213

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201820636662.1U Expired - Fee Related CN208154866U (en) 2018-04-28 2018-04-28 System for heating by utilizing waste heat of high-temperature coal tar distillation warm water system

Country Status (1)

Country Link
CN (1) CN208154866U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108375239A (en) * 2018-04-28 2018-08-07 中冶焦耐(大连)工程技术有限公司 Method and system for heating with waste heat from high temperature coal tar distillation warm water system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108375239A (en) * 2018-04-28 2018-08-07 中冶焦耐(大连)工程技术有限公司 Method and system for heating with waste heat from high temperature coal tar distillation warm water system

Similar Documents

Publication Publication Date Title
CN106765448A (en) A kind of energy-saving heating system for reducing heat supply return water temperature
CN203904327U (en) White liquor distilling apparatus
CN202769778U (en) Heat supply system for recovering open type circulation water waste heat of power plant
CN202101331U (en) Heat pump water-heating system using central air-conditioner cooling water and low-temperature flue gas afterheat
CN208154866U (en) System for heating by utilizing waste heat of high-temperature coal tar distillation warm water system
CN106439766A (en) Steam production device and direct compression type heat pump system
CN205664467U (en) Directly retrieve economizer that power plant's condenser waste heat is used for municipal heat supply
CN207018039U (en) The energy conserving system of the turbine generating system thermal efficiency is improved using absorption heat pump
CN209470286U (en) A kind of coupling heating plant using absorption type heat pump assembly recycling cooling water heat
CN106439783A (en) Heat energy efficient utilization system for recovering deaerator exhaust steam and heating fan heater simultaneously
CN207179770U (en) A kind of Combined Cycle Unit Gateway Station in Heating Network system based on SSS clutches
CN206094022U (en) Heat energy efficient utilization system for recovering deaerator exhaust steam and heating fan heater simultaneously
CN206709049U (en) A kind of thermal power plant waste heat comprehensive utilization system
CN109595669A (en) Solar energy waste-heat recovery device
CN109595673A (en) The united heat device of postposition solar energy waste-heat recovery device and lithium bromide heat pump
CN108375239A (en) Method and system for heating with waste heat from high temperature coal tar distillation warm water system
CN109695970A (en) The integrated collection system of float glass waste heat and solar heat
CN109682108A (en) Float glass waste-heat recovery device
CN109595675A (en) The integrated collection system of solar heat and lithium bromide heat pump heating
CN109631396A (en) The mixed water of combined heat and power and divide ability of swimming heat pump heating device
CN109631400A (en) Use the waste heat recycling of solar energy waste heat concurrent heating and heating installation
CN202730092U (en) Energy-saving heating system of coking crude benzol storage tank
CN109631402A (en) The float glass waste-heat recovery device of lithium bromide heat pump heating
CN109695969A (en) The lithium bromide heat pump heating device that the heat pump of power plant's cogeneration of heat and power is mixed with plate heat exchanger
CN208419274U (en) A kind of power station auxiliary cooling water afterheat utilization system

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20181127