CN207299005U - A kind of residual neat recovering system based on dividing wall type heat exchanger - Google Patents

A kind of residual neat recovering system based on dividing wall type heat exchanger Download PDF

Info

Publication number
CN207299005U
CN207299005U CN201721114784.6U CN201721114784U CN207299005U CN 207299005 U CN207299005 U CN 207299005U CN 201721114784 U CN201721114784 U CN 201721114784U CN 207299005 U CN207299005 U CN 207299005U
Authority
CN
China
Prior art keywords
dividing wall
flue gas
heat
wall type
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.)
Active
Application number
CN201721114784.6U
Other languages
Chinese (zh)
Inventor
曹振华
胡士国
宁兆阳
秦延宁
王天飞
刘丽
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.)
Shandong Fuyuan Energy-Saving Environmental Protection Engineering Co Ltd
Original Assignee
Shandong Fuyuan Energy-Saving Environmental Protection Engineering 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 Shandong Fuyuan Energy-Saving Environmental Protection Engineering Co Ltd filed Critical Shandong Fuyuan Energy-Saving Environmental Protection Engineering Co Ltd
Priority to CN201721114784.6U priority Critical patent/CN207299005U/en
Application granted granted Critical
Publication of CN207299005U publication Critical patent/CN207299005U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/30Technologies for a more efficient combustion or heat usage

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

Heat recovery energy-saving technical field is the utility model is related to, particularly discloses a kind of residual neat recovering system based on dividing wall type heat exchanger.The dividing wall type flue gas heat-exchange unit of circulating water pipe in the residual neat recovering system based on dividing wall type heat exchanger, including termination connection flue gas system, internal setting, it is characterised in that:The inlet channel and outlet conduit of circulating water pipe in connection respectively are provided with the dividing wall type flue gas heat-exchange unit, inlet channel connects the interior circulating water outlet of absorption type heat pump assembly, outlet conduit connects the interior circulating water intake of absorption type heat pump assembly, and internal circulation water pump is provided with outlet conduit.The utility model is simple in structure, and design is reasonable, copes with operating mode change and adjusts in real time, both reduction smog discharge temperature had been realized, has recycled the purpose of heat, and the heat of recycling is endlessly transferred out, continuous service is enabled a system to, so as to reach energy-saving target.

Description

A kind of residual neat recovering system based on dividing wall type heat exchanger
(One)Technical field
Heat recovery energy-saving technical field is the utility model is related to, more particularly to a kind of waste heat based on dividing wall type heat exchanger returns Receipts system.
(Two)Background technology
In recent years, with the exacerbation of air pollution and carrying forward vigorously for national energy-saving emission reduction policy, coal-burning boiler is Substituted by natural gas boiler, contain substantial amounts of water vapour in the flue gas discharged after combustion of natural gas, the condensation of water vapour in flue gas Latent heat accounts for the 10%-11% of natural gas low heat value, if can utilize this condensing units, can improve natural gas utilizes effect Rate.For the exhaust gas temperature of existing gas fired-boiler mostly at 90 DEG C -150 DEG C, so high exhaust gas temperature causes a large amount of waste heats to be dissipated in In environment.And this heat is recycled, it is necessary to flue-gas temperature is cooled to below flue gas dew point temperature, flue gas dew point temperature is 57 DEG C or so, but in China central heating field, heat supply network return water temperature generally more than 50 DEG C, if directly and flue gas heat exchange, only Sensible heat and a small amount of latent heat, energy-saving effect and unobvious in energy recovered flue gas.
Intermediate circulating water then can be cooled to 20 DEG C -30 DEG C by absorption heat pump by driving heat source, the recirculated water of this temperature There is larger heat transfer temperature difference with flue gas, sensible heat and latent heat in flue gas can be fully absorbed, so as to fulfill to more low-grade heat Amount recycling and conveying, play the role of linking in heat recovery and utilization process.
(Three)The content of the invention
The utility model is in order to make up for the deficiencies of the prior art, there is provided a kind of simple in structure, reduction smog discharge temperature, The residual neat recovering system based on dividing wall type heat exchanger of Mist heat recovering.
The utility model is achieved by the following technical solution:
Followed in a kind of residual neat recovering system based on dividing wall type heat exchanger, including termination connection flue gas system, internal setting The dividing wall type flue gas heat-exchange unit of ring water pipe, it is characterised in that:It is provided with the dividing wall type flue gas heat-exchange unit and is followed respectively in connection The inlet channel and outlet conduit of ring water pipe, inlet channel connect the interior circulating water outlet of absorption type heat pump assembly, outlet conduit The interior circulating water intake of absorption type heat pump assembly is connected, internal circulation water pump is installed on outlet conduit.
The utility model realizes the recycling of heat by dividing wall type flue gas heat-exchange unit, and heat is realized by absorption type heat pump assembly The transfer of amount utilizes, and internal circulation water pump provides the power of interior circulation water circulation use, and inlet channel and outlet conduit are as system Necessary connecting component, be the essential part of system.
The more excellent technical solution of the utility model is:
Valve is installed on the outlet conduit, the flow for recirculated water in being adjusted according to actual operating state.
The absorption type heat pump assembly is connected with driving heat source and outer net circulating water system, is easy to implement in absorption heat pump Heat exchange occurs in unit, transfers heat to outer net circulating water, realizes that the transfer of heat utilizes.
The dividing wall type flue gas heat-exchange unit bottom is provided with flue gas condensing water outlet, easy in time go out condensed water elimination Go.
The flow direction of flue gas and the flow direction of interior recirculated water are on the contrary, effectively improve in the dividing wall type flue gas heat-exchange unit Heat exchanger effectiveness of the interior recirculated water in flow process.
Dividing wall type flue gas heat-exchange unit be it is a kind of can with recovered flue gas sensible heat and the indirect type heat exchanger of latent heat, have it is corrosion-resistant Design structure, can be effectively resistant to the corrosion of flue gas condensing water, be designed using split structure, utilize detachable maintaining.
Flue gas enters from the side of dividing wall type flue gas heat-exchange unit, exchanges heat with the recirculated water in interior circulating water pipe, in flue gas Heat is absorbed by recirculated water, and when flue-gas temperature is cooled to below dew-point temperature, the water vapour in flue gas starts to condense heat release, cold Condensate flow to condensation water tank by the flue gas condensing water drainpipe of exchanger base.The flue gas after temperature is reduced through dividing wall type flue gas Heat exchanger exit is arranged to air to chimney.
Absorb the recirculated water after heat and reach internal circulation water pump through outlet conduit, moved after being pressurizeed by internal circulation water pump Power, to overcome the resistance of whole cyclic process.Interior recirculated water after pressurization enters absorption type heat pump assembly through outlet conduit again, Heat exchange occurs for the recirculated water in absorption type heat pump assembly with outer net, transfers heat to the recirculated water of outer net, realizes heat Transfer utilizes.Exothermic interior circulating water temperature reduces, and the ability for absorbing flue gas heat is regained, then through inlet channel Dividing wall type flue gas heat-exchange unit is returned, participates in heat transfer process again.
The utility model is simple in structure, and design is reasonable, copes with operating mode change and adjusts in real time, had both realized reduction flue gas Exhaust temperature, recycles the purpose of heat, and the heat of recycling is endlessly transferred out, and enables a system to continuous service, So as to reach energy-saving target.
(Four)Brief description of the drawings
The utility model will be further described below with reference to the accompanying drawings.
Fig. 1 is the structure diagram of the utility model.
In figure, 1 dividing wall type flue gas heat-exchange unit, 2 valves, 3 internal circulation water pumps, 4 absorption type heat pump assemblys, 5 inlet channels, 6 Outer net circulating water system, 7 driving heat sources.
(Five)Embodiment
Attached drawing is a kind of specific embodiment of the utility model.The embodiment includes termination connection flue gas system, inside is set The dividing wall type flue gas heat-exchange unit 1 of interior circulating water pipe is put, recirculated water in connection respectively is provided with the dividing wall type flue gas heat-exchange unit 1 The inlet channel 5 and outlet conduit of pipe, inlet channel 5 connect the interior circulating water outlet of absorption type heat pump assembly 4, and outlet conduit connects The interior circulating water intake of absorption type heat pump assembly 4 is connect, internal circulation water pump 3 is installed on outlet conduit;Pacify on the outlet conduit Equipped with valve 2;The absorption type heat pump assembly 4 is connected with driving heat source 7 and outer net circulating water system 6;The dividing wall type flue gas 1 bottom of heat exchanger is provided with flue gas condensing water outlet;The flow direction of flue gas is followed with interior in the dividing wall type flue gas heat-exchange unit 1 The flow direction of ring water is opposite.
Using the residual neat recovering system of the utility model, flue gas of the flue gas first from 1 side of dividing wall type flue gas heat-exchange unit enters Mouth enters, and after the interior recirculated water heat exchange in interior circulating water pipe, is discharged from the opposite side of dividing wall type flue gas heat-exchange unit 1.Flue gas with Interior recirculated water reverse flow, ensures larger heat transfer temperature difference and preferable heat transfer effect.Flue gas is warm under the cooling of interior recirculated water Degree is lasting to be reduced, and is collected after the water vapour condensation in flue gas from the flue gas condensing water outlet outflow of bottom.After being heated Interior recirculated water is through valve 2, after being pressurizeed by internal circulation water pump 3, into absorption type heat pump assembly 4, and under the driving of driving heat source 7, Heat is extracted by interior recirculated water, and is transferred to outer net circulating water system 6.Interior recirculated water through inlet channel 5, returns again again Heat exchange is participated in dividing wall type flue gas heat-exchange unit 1.Outer circulation water from outer net circulating water system 6 passes through absorption type heat pump assembly 4 internal heat process, absorbs the heat of heat and driving heat source 7 from interior recirculated water, delivers heat to outer net, reach The purpose of heat recovery and utilization.

Claims (5)

  1. A kind of 1. circulation in residual neat recovering system based on dividing wall type heat exchanger, including termination connection flue gas system, internal setting The dividing wall type flue gas heat-exchange unit of water pipe(1), it is characterised in that:The dividing wall type flue gas heat-exchange unit(1)On be provided with and connect respectively The inlet channel of interior circulating water pipe(5)And outlet conduit, inlet channel(5)Connect absorption type heat pump assembly(4)Interior recirculated water Outlet, outlet conduit connection absorption type heat pump assembly(4)Interior circulating water intake, internal circulation water pump is installed on outlet conduit (3).
  2. 2. the residual neat recovering system according to claim 1 based on dividing wall type heat exchanger, it is characterised in that:The outlet pipe Valve is installed on road(2).
  3. 3. the residual neat recovering system according to claim 1 based on dividing wall type heat exchanger, it is characterised in that:It is described absorption Heat pump unit(4)It is connected with driving heat source(7)And outer net circulating water system(6).
  4. 4. the residual neat recovering system according to claim 1 based on dividing wall type heat exchanger, it is characterised in that:The dividing wall type Flue gas heat-exchange unit(1)Bottom is provided with flue gas condensing water outlet.
  5. 5. the residual neat recovering system according to claim 1 based on dividing wall type heat exchanger, it is characterised in that:The dividing wall type Flue gas heat-exchange unit(1)The flow direction of interior flue gas is opposite with the flow direction of interior recirculated water.
CN201721114784.6U 2017-09-01 2017-09-01 A kind of residual neat recovering system based on dividing wall type heat exchanger Active CN207299005U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721114784.6U CN207299005U (en) 2017-09-01 2017-09-01 A kind of residual neat recovering system based on dividing wall type heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721114784.6U CN207299005U (en) 2017-09-01 2017-09-01 A kind of residual neat recovering system based on dividing wall type heat exchanger

Publications (1)

Publication Number Publication Date
CN207299005U true CN207299005U (en) 2018-05-01

Family

ID=62438541

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721114784.6U Active CN207299005U (en) 2017-09-01 2017-09-01 A kind of residual neat recovering system based on dividing wall type heat exchanger

Country Status (1)

Country Link
CN (1) CN207299005U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109489255A (en) * 2018-11-22 2019-03-19 青岛国信海天中心建设有限公司 A kind of flue gas condensing heat recovery apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109489255A (en) * 2018-11-22 2019-03-19 青岛国信海天中心建设有限公司 A kind of flue gas condensing heat recovery apparatus

Similar Documents

Publication Publication Date Title
CN205383632U (en) Natural gas waste heat of boiler flue gas cascade utilization system
CN207350355U (en) A kind of flue gas in power station boiler condenses reheating energy conserving system
CN109798534A (en) A kind of residual heat from boiler fume utilizes and takes off white integral system
CN105423595A (en) Heating efficient energy-saving direct combustion type lithium bromide absorbing type cold and hot water unit
CN105423593A (en) Heating normal-temperature smoke exhaust direct combustion type lithium bromide absorbing type cold and hot water unit
CN206929794U (en) The boiler exhaust gas total heat recoveries of nicotinic acids a kind of and flue gas disappear white device
CN205825498U (en) A kind of system of multistage recovery combustion gas fume afterheat
CN205245217U (en) System is utilized to steam turbine exhaust steam waste heat coupling waste heat of boiler flue gas degree of depth
CN207299005U (en) A kind of residual neat recovering system based on dividing wall type heat exchanger
CN202002316U (en) Built-in vacuum hot water boiler with condensing heat recovery
CN207214097U (en) A kind of coal-burning boiler based on smoke evacuation vapor internal-circulation type condensing units
CN208365564U (en) A kind of boiler smoke energy conservation disappears white device
CN208635370U (en) A kind of environment-friendly high-efficiency flue gas type lithium bromide absorption cold, Hot water units
CN209116822U (en) A kind of residual heat of electric power plant and clean energy resource utilization system
CN204574092U (en) Boiler tail flue gas waste heat complicated utilization system
CN206478721U (en) A kind of Circulating Cooling Water of Power Plant condensation waste heat utilizes system
CN201815457U (en) Energy-saving curing oven and drying oven system
CN205807384U (en) A kind of MGGH condensation water heating system
CN201293568Y (en) Hot blast intermediate reflux low temperature corrosion resistant air preheater
CN205402669U (en) Hot tube -type evaporator absorption heat pump residual heat from flue gas system
CN205860072U (en) A kind of flue gas waste heat recovery system
CN204358990U (en) A kind of gas fired-boiler smoke heat energy recycling system
CN205279508U (en) Cold, hot water unit of high -efficient flue gas hot water type lithium bromide absorption formula of heating
CN205174432U (en) Boiler air inlet preheating device with amortization function
CN204534546U (en) Biomass boiler environmental protection and energy saving control system

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant