CN103712373A - Waste heat recovery system aiming at intermittent heating production of waste water source containing impurities - Google Patents
Waste heat recovery system aiming at intermittent heating production of waste water source containing impurities Download PDFInfo
- Publication number
- CN103712373A CN103712373A CN201410008504.8A CN201410008504A CN103712373A CN 103712373 A CN103712373 A CN 103712373A CN 201410008504 A CN201410008504 A CN 201410008504A CN 103712373 A CN103712373 A CN 103712373A
- Authority
- CN
- China
- Prior art keywords
- water
- plate type
- heat exchanger
- pump
- type heat
- 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
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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
Abstract
The invention provides a waste heat recovery system aiming at intermittent heating production of a waste water source containing impurities. The waste heat recovery system aiming at the intermittent heating production of the waste water source containing the impurities comprises an absorption heat pump, a front water storage tank, a filter device, a water pump, an air pre-heater, a rear water storage tank and two plate heat exchanging devices. The input material of a generator part of the absorption heat pump is external connected steam of chemical plants, and the output material of the generator part of the absorption heat pump is condensate water. Hot waste water is connected with the first plate heat exchanging device after passing through the front water storage tank and the filter device, is output to the second plate heat exchanging device, and is changed into low-temperature waste water through heat exchange again. Tap water forms circulation water through an evaporator of the absorption heat pump, the water pump and the plate heat exchanging devices. Clear water forms circulation clear water through the first plate heat exchanging device, an absorber, a condenser, the water pump, the rear water storage tank and the air pre-heater, the circulation clear water carries out heat exchange in the air pre-heater through the absorption heat pump, and cold air is heated into hot air to meet user requirements. The waste heat recovery system aiming at the intermittent heating production of the waste water source containing the impurities has the advantages of being high in heat recovery efficiency and the like.
Description
Technical field
The present invention relates to a kind of chemical plant waste-heat recovery device, relate in particular to the residual neat recovering system that impure intermittence heating is produced for waste water source.
Background technology
For chemical plant, the low-temperature wastewater of its generation is by treatment system or directly discharge the huge heat-energy losses of meeting formation, makes chemical plant capacity usage ratio low, not only causes mass energy waste, has also seriously polluted environment simultaneously.Along with the development of heat pump techniques, the particularly appearance of large high-temperature water resource heat pump, makes chemical plant low-temperature wastewater waste heat recovery will become possibility.In addition, absorption heat pump formula is to rely on driving heat source operation, the temperature that absorbs low-temperature heat source water is transferred to the equipment of middle warm water, it when unit operation, is the temperature that continuously absorbs low-temperature heat source, but when there is cutout in low-temperature heat source water, namely can not provide continuously heat, and unit is now still in continuous heat absorption, the temperature of the heat exchanger of absorption heat pump low temperature water inlet front end will sharply decline so, until residual water freezing in pipe, after water build-ups ice, volume can become large, thereby burst low-temperature heat exchange device, whole system paralysis, and there is the problem of a large amount of impurity in the spent hot water in current chemical plant, greatly affect the efficiency of plate type heat exchanger, cannot make full use of existing spent hot water's heat.And existing hot-air acquisition methods is to obtain by the new wind of Steam Heating, this part steam need to spend to buy.
Summary of the invention
Technology of the present invention is dealt with problems and is: the problem for existing for the discontinuous residual neat recovering system by air heat of waste water source in prior art, provides a kind of residual neat recovering system.
Technical solution of the present invention is: a kind of residual neat recovering system that impure intermittence heating is produced for waste water source, comprise absorption heat pump, front water tank, filter, air preheater, water pump, rear water tank, the first plate type heat exchanger and the second plate type heat exchanger, wherein absorption heat pump is divided into generator part, evaporator section, absorber part and condenser portion, generator part be input as chemical plant steam-out (SO), be output as condensed water; The output of evaporator section is connected with the second plate type heat exchanger, evaporator section be input as running water, running water forms recirculated water by evaporimeter, water pump and second plate type heat exchanger of absorption heat pump, this recirculated water absorbs heat from the second plate type heat exchanger, bring heat into after evaporimeter release heat, and then get back to the second plate type heat exchanger heat absorption; After the spent hot water in chemical plant stores by front water tank, become continuous spent hot water, pass through again filter by impurity filtering, input as the first plate type heat exchanger, spent hot water after the cooling of the output of the first plate type heat exchanger is as the input of the second plate type heat exchanger, enters the spent hot water who becomes low temperature after secondary heat exchange and discharges; After low temperature clear water once heats up after the first plate type heat exchanger, as the input of the absorber part of absorption heat pump, the output of absorber part is connected with the input of condenser; Clear water after once heating up is after absorption heat pump carries out secondary temperature elevation, again through forming circulation clear water after water tank and air preheater later, circulation clear water heats cold wind (new wind) in air preheater, output warm-air supply user, to meet consumers' demand, save this part new wind-warm syndrome and risen the steam of required consumption, reached energy-conservation object.
The present invention's advantage is compared with prior art: the present invention realizes waste heat recovery by the heat exchange method of absorption heat pump, reclaim the spent hot water in chemical plant, before utilizing, water tank becomes continuous state by waste water, then after being connected with plate type heat exchanger, tap water heating is formed to recirculated water, clear water is undertaken after secondary temperature elevation by the first plate type heat exchanger and absorption heat pump, by rear water tank and water pump and air preheater, by cold air heating, it is hot blast, to meet the demand of user to technique, whole system has been realized abundant recycling and the heat supply of waste water by two plate type heat exchangers, improve heat utilization rate, effectively save the energy.
Accompanying drawing explanation
Fig. 1 is the residual neat recovering system structural representation that impure intermittence heating is produced for waste water source of the present invention.
The specific embodiment
A kind of residual neat recovering system that impure intermittence heating is produced for waste water source, as shown in Figure 1, comprise absorption heat pump, front water tank, filter, air preheater, water pump, rear water tank, the first plate type heat exchanger and the second plate type heat exchanger, wherein absorption heat pump is divided into generator part, evaporator section, absorber part and condenser portion, generator part be input as chemical plant steam-out (SO), be output as condensed water; The output of evaporator section is connected with the second plate type heat exchanger, evaporator section be input as running water, running water forms recirculated water by evaporimeter, water pump and second plate type heat exchanger of absorption heat pump, this recirculated water absorbs heat from the second plate type heat exchanger, bring heat into after evaporimeter release heat, and then get back to the second plate type heat exchanger heat absorption; After the spent hot water of chemical plant 60 degree or higher temperature stores by front water tank, become continuous spent hot water, pass through again filter by impurity filtering, input as the first plate type heat exchanger, after the cooling of the output of the first plate type heat exchanger 40 degree spent hot water, as the input of the second plate type heat exchanger, enters the spent hot water who becomes about low temperature 20 degree after secondary heat exchange and discharges; Low temperature clear water is as the input of the absorber part of absorption heat pump, and the output of absorber part is connected with the input of condenser; After low temperature 20 degree (mean annual temperature) clear water once heat up after the first plate type heat exchanger, become 60 degree left and right, as the input of the absorber part of absorption heat pump, the output of absorber part is connected with the input of condenser; Clear water after once heating up carries out secondary temperature elevation through absorption heat pump and becomes after 85～90 degree, again through forming circulation clear water after water tank and air preheater later, circulation clear water heats cold wind in air preheater, it by the cold air heating of 20 degree, is the hot blast of 70 degree, then supply with user, to meet user's requirement.
It should be noted that, the water tank of that side that is positioned at the evaporator section of absorption heat pump is called front water tank, and the water tank of that side that is positioned at the condenser portion of absorption heat pump is called rear water tank.
The content not being described in detail in description of the present invention belongs to the known prior art of professional and technical personnel in the field.
Claims (1)
1. one kind is heated for the impure intermittence of waste water source the residual neat recovering system of producing, it is characterized in that: comprise absorption heat pump, front water tank, filter, air preheater, water pump, rear water tank, the first plate type heat exchanger and the second plate type heat exchanger, wherein absorption heat pump is divided into generator part, evaporator section, absorber part and condenser portion, generator part be input as chemical plant steam-out (SO), be output as condensed water; The output of evaporator section is connected with the second plate type heat exchanger, evaporator section be input as running water, running water forms recirculated water by evaporimeter, water pump and second plate type heat exchanger of absorption heat pump, this recirculated water absorbs heat from the second plate type heat exchanger, bring heat into after evaporimeter release heat, and then get back to the second plate type heat exchanger heat absorption; After the spent hot water in chemical plant stores by front water tank, become continuous spent hot water, pass through again filter by impurity filtering, input as the first plate type heat exchanger, spent hot water after the cooling of the first plate type heat exchanger output is as the input of the second plate type heat exchanger, enters the spent hot water who becomes low temperature after secondary heat exchange and discharges; After low temperature clear water once heats up after the first plate type heat exchanger, as the input of the absorber part of absorption heat pump, the output of absorber part is connected with the input of condenser; Clear water after once heating up is after absorption heat pump carries out secondary temperature elevation, then through forming circulation clear water after water tank and air preheater later, circulation clear water heats cold wind in air preheater, and output warm-air supply user, to meet consumers' demand.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410008504.8A CN103712373A (en) | 2014-01-06 | 2014-01-06 | Waste heat recovery system aiming at intermittent heating production of waste water source containing impurities |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410008504.8A CN103712373A (en) | 2014-01-06 | 2014-01-06 | Waste heat recovery system aiming at intermittent heating production of waste water source containing impurities |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103712373A true CN103712373A (en) | 2014-04-09 |
Family
ID=50405548
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410008504.8A Pending CN103712373A (en) | 2014-01-06 | 2014-01-06 | Waste heat recovery system aiming at intermittent heating production of waste water source containing impurities |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103712373A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108548323A (en) * | 2018-05-16 | 2018-09-18 | 江苏必领能源科技有限公司 | Recuperation of heat high temperature heat pump system |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6076369A (en) * | 1998-01-28 | 2000-06-20 | Mitsubishi Heavy Industries, Ltd. | Evaporative concentration apparatus for waste water |
| CN2929596Y (en) * | 2006-07-17 | 2007-08-01 | 祝建军 | Absorptive heat pump system for recovering waste heat from power plant, printing and dyeing, oil field and pharmaceutical industries |
| CN201155887Y (en) * | 2008-01-04 | 2008-11-26 | 广州德能热源设备有限公司 | Sewage water source heat pump hot water units |
| CN101799207A (en) * | 2010-03-05 | 2010-08-11 | 清华大学 | System and method for recycling waste heat of bath sewage by utilizing absorption heat pump |
| CN201569208U (en) * | 2009-09-28 | 2010-09-01 | 北京神舟克莱新能源科技有限公司 | Residual heat reclamation device in petroleum industry |
| CN202869075U (en) * | 2012-10-29 | 2013-04-10 | 郑州恒博科技有限公司 | Waste heat recovery absorption heat pump system special for chemical fiber factory |
-
2014
- 2014-01-06 CN CN201410008504.8A patent/CN103712373A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6076369A (en) * | 1998-01-28 | 2000-06-20 | Mitsubishi Heavy Industries, Ltd. | Evaporative concentration apparatus for waste water |
| CN2929596Y (en) * | 2006-07-17 | 2007-08-01 | 祝建军 | Absorptive heat pump system for recovering waste heat from power plant, printing and dyeing, oil field and pharmaceutical industries |
| CN201155887Y (en) * | 2008-01-04 | 2008-11-26 | 广州德能热源设备有限公司 | Sewage water source heat pump hot water units |
| CN201569208U (en) * | 2009-09-28 | 2010-09-01 | 北京神舟克莱新能源科技有限公司 | Residual heat reclamation device in petroleum industry |
| CN101799207A (en) * | 2010-03-05 | 2010-08-11 | 清华大学 | System and method for recycling waste heat of bath sewage by utilizing absorption heat pump |
| CN202869075U (en) * | 2012-10-29 | 2013-04-10 | 郑州恒博科技有限公司 | Waste heat recovery absorption heat pump system special for chemical fiber factory |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108548323A (en) * | 2018-05-16 | 2018-09-18 | 江苏必领能源科技有限公司 | Recuperation of heat high temperature heat pump system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203190489U (en) | Efficient lithium bromide absorption heat pump heat exchanger unit | |
| CN103808060B (en) | Band flash vessel two-stage absorbs Equations of The Second Kind lithium bromide absorption type heat pump unit | |
| CN105783023A (en) | Device and method for driving air heater through absorption type heat pump | |
| CN103727512A (en) | Waste heat recovering system capable of continuously generating steam aiming at impure waste water resources | |
| CN203704433U (en) | Two-stage lithium bromide absorption heat transformer unit with flash evaporator | |
| CN203159268U (en) | solar air conditioning seawater desalination system | |
| CN202470543U (en) | Warming type absorption heat pump with middle-temperature heat source in series | |
| CN103712368A (en) | Waste heat recovery system aiming at discontinuous waste water source and discontinuous process water | |
| CN203771678U (en) | Residual heat recovery system for air heating by discontinuous hot waste water source | |
| CN110567190B (en) | Vapor compression type absorption heat pump | |
| CN203704434U (en) | Two-stage lithium bromide absorption heat transformer unit with refrigerant water preheater | |
| CN103808059B (en) | Secondary generation secondary absorbs Equations of The Second Kind lithium bromide absorption type heat pump unit | |
| CN103808058B (en) | Band water as refrigerant preheater two-stage Equations of The Second Kind lithium bromide absorption type heat pump unit | |
| CN103727700A (en) | Waste heat recovering system aiming at discontinuous and impure waste water resources | |
| CN203771687U (en) | Residual heat recovery system for continuous air heating by discontinuous waste water source | |
| CN103712373A (en) | Waste heat recovery system aiming at intermittent heating production of waste water source containing impurities | |
| CN203771781U (en) | Residual heat recovery system for steam preparation | |
| CN203704432U (en) | Secondary-generating and secondary-absorbing second type lithium bromide absorption type heat pump unit | |
| CN203771773U (en) | Waste heat recycling system heating air | |
| CN202993661U (en) | Absorption type energy recovery and quality improving device | |
| CN104229913B (en) | A kind of solar water distiller all-in-one | |
| CN203771801U (en) | Residual heat recovery system for steam preparation of dyeing factory | |
| CN203771802U (en) | Residual heat recovery system for continuous air heating for chemical plant | |
| CN203771774U (en) | Residual heat recovery system for discontinuous low-temperature waste water | |
| CN203771772U (en) | Residual heat recovery system for discontinuous impurity-containing waste water source of chemical plant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C53 | Correction of patent of invention or patent application | ||
| CB02 | Change of applicant information |
Address after: 311202, No. 1, building 237, No. five, No. 3 Hing Road, Xiaoshan District, Zhejiang, Hangzhou Applicant after: Hangzhou Environment Technology Co., Ltd. Address before: 311202, No. 1, building 237, No. five, No. 3 Hing Road, Xiaoshan District, Zhejiang, Hangzhou Applicant before: HANGZHOU WORUN ENERGY-SAVING TECHNOLOGY CO., LTD. |
|
| COR | Change of bibliographic data |
Free format text: CORRECT: APPLICANT; FROM: HANGZHOU WORUN ENERGY-SAVING TECHNOLOGY CO., LTD. TO: HANGZHOU WORUI ENVIRONMENT TECHNOLOGY CO., LTD. |
|
| DD01 | Delivery of document by public notice |
Addressee: Hangzhou Environment Technology Co., Ltd. Document name: Notification that Application Deemed to be Withdrawn |
|
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20140409 |