CN203848505U - Device for recovering condensation heat energy of gas boiler flue gas by means of heat pump - Google Patents
Device for recovering condensation heat energy of gas boiler flue gas by means of heat pump Download PDFInfo
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- CN203848505U CN203848505U CN201420157019.2U CN201420157019U CN203848505U CN 203848505 U CN203848505 U CN 203848505U CN 201420157019 U CN201420157019 U CN 201420157019U CN 203848505 U CN203848505 U CN 203848505U
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- circulating water
- heat exchanger
- secondary cycle
- pump
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 54
- 239000003546 flue gas Substances 0.000 title claims abstract description 54
- 238000009833 condensation Methods 0.000 title claims abstract description 43
- 230000005494 condensation Effects 0.000 title claims abstract description 43
- 239000007789 gas Substances 0.000 title claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 252
- 238000010438 heat treatment Methods 0.000 claims description 27
- 239000000779 smoke Substances 0.000 claims description 26
- 238000005086 pumping Methods 0.000 claims description 24
- 238000001816 cooling Methods 0.000 claims description 14
- 230000007797 corrosion Effects 0.000 claims description 8
- 238000005260 corrosion Methods 0.000 claims description 8
- 238000007599 discharging Methods 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 4
- 238000011084 recovery Methods 0.000 abstract description 13
- 230000001502 supplementing effect Effects 0.000 abstract 2
- 239000003517 fume Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000009834 vaporization Methods 0.000 description 3
- 230000008016 vaporization Effects 0.000 description 3
- 239000000567 combustion gas Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 230000003020 moisturizing effect Effects 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 239000003929 acidic solution Substances 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000009514 concussion Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Classifications
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- 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
- Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
-
- 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]
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model relates to a device for recovering the condensation heat energy of gas boiler flue gas by means of a heat pump, wherein a device with a high heat energy recovery rate and used for recovering the condensation heat energy of gas boiler flue gas is inexistent presently. The device disclosed by the utility model comprises an efficient condensation heat exchanger, a primary circulating water heat exchanger outlet tube, a flue gas inlet tube and a flue gas outlet tube, and is characterized by further comprising a heat pump unit, a primary circulating water heat pump inlet tube, a primary circulating water heat pump outlet tube, a primary circulating water pump, a domestic hot water taking tube, a primary circulating water supplementing tube, a secondary circulating water pump, a secondary circulating water heat pump inlet tube and a secondary circulating water heat pump outlet tube, wherein one end of the primary circulating water heat pump outlet tube and one end of the primary circulating water supplementing tube are connected to the other end of the primary circulating water heat pump inlet tube; the secondary circulating water pump is installed on the secondary circulating water heat pump inlet tube; the outlet thermometer of the secondary circulating water pump is installed on the secondary circulating water heat pump outlet tube. The device disclosed by the utility model is high in heat energy recovery rate.
Description
Technical field
The utility model relates to a kind of device that reclaims gas fired-boiler flue gas to condense thermal energy, especially relates to the device that reclaims gas fired-boiler flue gas to condense thermal energy with heat pump mode.
Background technology
Gas fired-boiler is discharged fume generally more than 150 DEG C, in flue gas, contain the steam that volume fraction reaches 15%-20%, this part steam is superheat state, and its latent heat of vaporization is not used, and these steam that are superheat state cause the massive losses of heat while discharge with flue gas.Gas fired-boiler progressively replaces coal-burning boiler at present, and gas fired-boiler is in urban life, production for hankering having obtained being widely used, and the condensate recycling device of gas fired-boiler starts to be applied.
It is mainly by single gas-water heat exchanger that gas fired-boiler condensation is at present reclaimed, flue-gas temperature is lowered the temperature, Mist heat recovering, if open day is on 04 11st, 2012, publication number is in the Chinese patent of CN102410550A, a kind of residual neat recovering system of condensing type anti-corrosive gas/oil-fired boiler is disclosed, this residual neat recovering system comprises a common heat exchange of heat pipe body and a solution spraying device, heat exchange of heat pipe body is passed to opposite side by the concussion transmission of heat pipe by heat by fume side by heat, in order to add hot-air or water, the solution of shower nozzle ejection is dispersed on the heat exchanger tube and heat exchanger inwall of fume side uniformly, eliminate the corrosion that in boiler smoke, steam condenses the weakly acidic solution forming.There are following 3 deficiencies in this mode of simply utilizing by single gas-water heat exchanger.
(1) hot water temperature is too low, only can be for domestic hot-water or heating boiler feedwater etc.
(2) flue-gas temperature cannot be down to enough low.The water of flue gas is mainly domestic hot-water or boiler feedwater, steam boiler confluent is few, hot-water boiler return water temperature is higher, all flue-gas temperature cannot be down to enough low, domestic hot-water needs leaving water temperature at 40-60 DEG C, exhaust gas temperature is mostly more than 60 DEG C, and in flue gas, the condensation ratio of steam is not high, and heat energy recovery rate is lower.
(3) in condensing heat exchanger, shower nozzle sprays solution and flue gas direct contact heat transfer, in flue gas, part heat is discharged with solution, has reduced energy recovery efficiency.
Also have now and adopt other modes to reclaim gas fired-boiler flue gas to condense thermal energy, if open day is on 08 29th, 2012, publication number is in the Chinese patent of CN102650431A, a kind of combustion gas fume afterheat step recoverying and utilizing method is disclosed, this combustion gas fume afterheat step recoverying and utilizing method utilizes the series connection of two kinds of different heat transfer modes of the gentle water direct heat-exchange of air water indirect heat exchange, low grade heat energy in step recovered flue gas, for healed water temperature continuance lifting, healed water temperature is through twice continuance lifting, temperature is elevated to 60-100 DEG C, as steam boiler moisturizing, waste heat boiler moisturizing, other process waters or domestic hot-water use, this system need consume high-grade electric energy, and function is comparatively single.
In sum, also do not have now a kind of heat energy recovery rate high, the water temperature of a recirculated water, can be fully cooling by flue gas at 15-30 DEG C, flue gas is down to below dew point, fully the device of the recovery gas fired-boiler flue gas to condense thermal energy of the sensible heat of recovered flue gas and the latent heat of vaporization of steam.
Utility model content
The purpose of this utility model is to overcome above shortcomings in prior art, and provide a kind of reasonable in design, heat energy recovery rate is high, the water temperature of a recirculated water is at 15-30 DEG C, can flue gas is fully cooling, flue gas is down to below dew point, fully the device with heat pump mode recovery gas fired-boiler flue gas to condense thermal energy of the sensible heat of recovered flue gas and the latent heat of vaporization of steam.
The technical scheme in the invention for solving the above technical problem is: should comprise high-efficiency condensation heat exchanger with the device of heat pump mode recovery gas fired-boiler flue gas to condense thermal energy, a Heat Exchanger in Circulating Water System outlet, a Heat Exchanger in Circulating Water System inlet tube, smoke inlet pipe and smoke outlet tube, be provided with condensing heat exchanger condensate water discharging mouth in described high-efficiency condensation heat exchanger, smoke inlet, exhanst gas outlet, a recirculated water entrance and a circulating water outlet, one end of described smoke inlet pipe and one end of smoke outlet tube are connected on the smoke inlet and exhanst gas outlet of high-efficiency condensation heat exchanger, one end of one end of a described Heat Exchanger in Circulating Water System outlet and a Heat Exchanger in Circulating Water System inlet tube is connected on a circulating water outlet and a recirculated water entrance of high-efficiency condensation heat exchanger, and its design feature is: also comprise source pump, a Heat Exchanger in Circulating Water System outlet temperature meter, a circulating water flow meter, a circulating water heating pumping intake piping, a circulating water heating pump discharge pipe, a water circulating pump, a Heat Exchanger in Circulating Water System inlet temperature meter, domestic hot-water's intake pipe, a circulating cooling make-up water pipe, secondary cycle water pump, secondary cycle water return water temperature meter, secondary cycle hydro-thermal pumping intake piping, secondary cycle hydro-thermal pump discharge pipe, secondary cycle water ga(u)ge and secondary cycle hydro-thermal pump discharge thermometer, a described water circulating pump and a Heat Exchanger in Circulating Water System inlet temperature meter are installed on a Heat Exchanger in Circulating Water System inlet tube, and a described Heat Exchanger in Circulating Water System outlet temperature meter and a circulating water flow meter are installed on a Heat Exchanger in Circulating Water System outlet, one end of one end of a described circulating water heating pump discharge pipe and a circulating cooling make-up water pipe is all connected on the other end of a Heat Exchanger in Circulating Water System inlet tube, and one end of one end of a described circulating water heating pumping intake piping and domestic hot-water's intake pipe is all connected on the other end of a Heat Exchanger in Circulating Water System outlet, in described source pump, be provided with recirculated water entrance one time, a circulating water outlet, secondary cycle water inlet and secondary cycle water out, the other end of the other end of a described circulating water heating pumping intake piping and a circulating water heating pump discharge pipe is connected on a recirculated water entrance and a circulating water outlet of source pump, one end of one end of described secondary cycle hydro-thermal pumping intake piping and secondary cycle hydro-thermal pump discharge pipe is connected on the secondary cycle water inlet and secondary cycle water out of source pump, described secondary cycle water pump and secondary cycle water return water temperature meter are installed on secondary cycle hydro-thermal pumping intake piping, described secondary cycle water ga(u)ge and secondary cycle hydro-thermal pump discharge thermometer are installed on secondary cycle hydro-thermal pump discharge pipe.Make thus reasonable in design of the present utility model, can flue gas is fully cooling, flue gas is down to below dew point, the rate of recovery of smoke heat energy is high, greatly reduces the corrosion to high-efficiency condensation heat exchanger, has extended the service life of equipment.
As preferably, the end heat-exchanging tube bundle along flow of flue gas direction in high-efficiency condensation heat exchanger described in the utility model adopts corrosion-resistant material.
As preferably, the base plate in high-efficiency condensation heat exchanger described in the utility model is downward-sloping gradually along flow of flue gas direction.
The utility model compared with prior art, has the following advantages and effect: 1. first adopt recirculated water of low temperature and the mode that high-temperature flue gas carries out heat exchange, be conducive to the temperature of high-temperature flue gas to drop to below 40 DEG C, improved the utilization rate of heat energy in flue gas; Re-use secondary cycle water and recirculated water carry out heat exchange mode by source pump, greatly improved the organic efficiency of heat energy, the temperature of secondary cycle water can have been improved to 50-90 DEG C, expanded the applicable surface of secondary cycle water.2. adopt high-efficiency condensation heat exchanger, high-efficiency condensation heat exchanger final stage heat-exchanging tube bundle adopts corrosion-resistant material, alleviate the cold end corrosion of high-efficiency condensation heat exchanger, high-efficiency condensation heat exchanger base plate is downward-sloping along flue gas direction, condensed water can be discharged in time, reduce corrosion and can avoid moisture evaporation to cause thermal loss.3. a circulating water temperature is controlled, and a general recirculated water leaving water temperature is controlled at 20 DEG C of left and right, and guarantee high-efficiency condensation heat exchanger exhanst gas outlet temperature can be down to below 40 DEG C, with abundant Mist heat recovering.4. according to physical condition different choice electric drive heat pump or absorption heat pump, secondary cycle coolant-temperature gage can be controlled between 50-90 DEG C.5. applicability is extensive, and because secondary cycle hydro-thermal energy quality is within life heating, production heat supply usable range, and temperature is controlled, thereby the scope of application is wider.6. reclaim gas fired-boiler flue gas to condense thermal energy with heat pump mode, adopt high-efficiency condensation heat exchanger by heat heat exchange to the time heat source water of flue gas, by heat pump by the heat heat exchange of a recirculated water to secondary cycle water, with respect to conventional condensing heat-exchange system, have that exhaust gas temperature is low, good energy-conserving effect, applicability are extensive, the reliable advantage of system stability.7. Heat Exchanger in Circulating Water System outlet connects respectively circulating water heating pumping intake piping and domestic hot-water's intake pipe, the water temperature of circulating water heating pumping intake piping and domestic hot-water's intake pipe requires different,, used flexibly by regulating a circulating water flow to control by a water circulating pump.
Brief description of the drawings
Fig. 1 is the structural representation that reclaims the device of gas fired-boiler flue gas to condense thermal energy in the utility model embodiment with heat pump mode.
In figure: 1-high-efficiency condensation heat exchanger, 2-source pump, Heat Exchanger in Circulating Water System outlet of 3-, Heat Exchanger in Circulating Water System outlet temperature meter of 4-, circulating water flow meter of 5-, circulating water heating pumping intake piping of 6-, circulating water heating pump discharge pipe of 7-, water circulating pump of 8-, Heat Exchanger in Circulating Water System inlet temperature meter of 9-, Heat Exchanger in Circulating Water System inlet tube of 10-, 11-smoke inlet pipe, 12-smoke outlet tube, 13-domestic hot-water intake pipe, circulating cooling make-up water pipe of 14-, 15-secondary cycle water pump, 16-secondary cycle water return water temperature meter, 17-secondary cycle hydro-thermal pumping intake piping, 18-secondary cycle hydro-thermal pump discharge pipe, 19-secondary cycle water ga(u)ge, 20-secondary cycle hydro-thermal pump discharge thermometer, 21-condensing heat exchanger condensate water discharging mouth.
Detailed description of the invention
Below in conjunction with accompanying drawing and by embodiment, the utility model is described in further detail, and following examples are to explanation of the present utility model and the utility model is not limited to following examples.
Embodiment.
Referring to Fig. 1, in the present embodiment, comprise high-efficiency condensation heat exchanger 1 with the device of heat pump mode recovery gas fired-boiler flue gas to condense thermal energy, source pump 2, a Heat Exchanger in Circulating Water System outlet 3, a Heat Exchanger in Circulating Water System outlet temperature meter 4, a circulating water flow meter 5, a circulating water heating pumping intake piping 6, a circulating water heating pump discharge pipe 7, a water circulating pump 8, a Heat Exchanger in Circulating Water System inlet temperature meter 9, a Heat Exchanger in Circulating Water System inlet tube 10, smoke inlet pipe 11, smoke outlet tube 12, domestic hot-water's intake pipe 13, a circulating cooling make-up water pipe 14, secondary cycle water pump 15, secondary cycle water return water temperature meter 16, secondary cycle hydro-thermal pumping intake piping 17, secondary cycle hydro-thermal pump discharge pipe 18, secondary cycle water ga(u)ge 19 and secondary cycle hydro-thermal pump discharge thermometer 20.
In high-efficiency condensation heat exchanger 1 in the present embodiment, be provided with condensing heat exchanger condensate water discharging mouth 21, smoke inlet, exhanst gas outlet, a recirculated water entrance and a circulating water outlet, one end of one end of smoke inlet pipe 11 and smoke outlet tube 12 is connected on the smoke inlet and exhanst gas outlet of high-efficiency condensation heat exchanger 1, and one end of one end of a Heat Exchanger in Circulating Water System outlet 3 and a Heat Exchanger in Circulating Water System inlet tube 10 is connected on a circulating water outlet and a recirculated water entrance of high-efficiency condensation heat exchanger 1.
A water circulating pump 8 and a Heat Exchanger in Circulating Water System inlet temperature meter 9 in the present embodiment are installed on a Heat Exchanger in Circulating Water System inlet tube 10, and a Heat Exchanger in Circulating Water System outlet temperature meter 4 and a circulating water flow meter 5 are installed on a Heat Exchanger in Circulating Water System outlet 3.One end of a circulating water heating pump discharge pipe 7 in the present embodiment and one end of a circulating cooling make-up water pipe 14 are all connected on the other end of a Heat Exchanger in Circulating Water System inlet tube 10, and one end of one end of a circulating water heating pumping intake piping 6 and domestic hot-water's intake pipe 13 is all connected on the other end of a Heat Exchanger in Circulating Water System outlet 3.
In source pump 2 in the present embodiment, be provided with one time recirculated water entrance, a circulating water outlet, secondary cycle water inlet and secondary cycle water out, in source pump 2, be provided with condenser and evaporimeter, the other end of the other end of a circulating water heating pumping intake piping 6 and a circulating water heating pump discharge pipe 7 is connected on a recirculated water entrance and a circulating water outlet of source pump 2, one end of one end of secondary cycle hydro-thermal pumping intake piping 17 and secondary cycle hydro-thermal pump discharge pipe 18 is connected on the secondary cycle water inlet and secondary cycle water out of source pump 2, secondary cycle water pump 15 and secondary cycle water return water temperature meter 16 are installed on secondary cycle hydro-thermal pumping intake piping 17, secondary cycle water ga(u)ge 19 and secondary cycle hydro-thermal pump discharge thermometer 20 are installed on secondary cycle hydro-thermal pump discharge pipe 18.
Under normal circumstances, the end heat-exchanging tube bundle along flow of flue gas direction in the high-efficiency condensation heat exchanger 1 in the utility model adopts corrosion-resistant material, and the base plate in high-efficiency condensation heat exchanger 1 is downward-sloping gradually along flow of flue gas direction.
While comprising the steps: to move with heat pump working condition with the method for heat pump mode recovery gas fired-boiler flue gas to condense thermal energy in the present embodiment, flue gas enters the interior cooling heat release of high-efficiency condensation heat exchanger 1 by smoke inlet pipe 11, flue gas after cooling is discharged high-efficiency condensation heat exchanger 1 by smoke outlet tube 12, now the temperature of flue gas, below 40 DEG C, flows out from condensing heat exchanger condensate water discharging mouth 21 after the water vapor condensation in flue gas, under the promotion of a water circulating pump 8, one time recirculated water enters through a Heat Exchanger in Circulating Water System inlet tube 10 heat energy that the interior absorption flue gas of high-efficiency condensation heat exchanger 1 is emitted, the temperature of a recirculated water is elevated between 15-30 DEG C, a recirculated water after intensification flows out high-efficiency condensation heat exchanger 1 through a Heat Exchanger in Circulating Water System outlet 3, and as the low-temperature heat source water of source pump 2, enter source pump 2 by a circulating water heating pumping intake piping 6 and carry out heat release, a recirculated water after cooling flows out by a circulating water heating pump discharge pipe 7, and under the promotion of a water circulating pump 8, again enter in high-efficiency condensation heat exchanger 1 heat absorption and heat up, so iterative cycles, secondary cycle water enters in source pump 2 by secondary cycle hydro-thermal pumping intake piping 17 under the promotion of secondary cycle water pump 15, absorb the heat energy that recirculated water is emitted, the temperature of secondary cycle water is elevated between 50-90 DEG C, secondary cycle water after intensification flows out source pump 2 through secondary cycle hydro-thermal pump discharge pipe 18, be delivered to user place and carry out heat release, and circulate under the promotion of secondary cycle water pump 15.
A recirculated water is by regulating exerting oneself of a water circulating pump 8 to change the water yield that enters high-efficiency condensation heat exchanger 1, thereby control inlet temperature and the outlet temperature of a recirculated water in high-efficiency condensation heat exchanger 1, the temperature of a recirculated water after heating up is controlled between 15-30 DEG C, thereby make the temperature of smoke outlet of high-efficiency condensation heat exchanger 1 low as much as possible, make full use of the waste heat in flue gas, and reduce environmental pollution; Secondary cycle water, according to the requirement of hot user's heat temperature, is chosen suitable source pump 2, controls the discharge of secondary cycle water pump 15, with return water temperature and the supply water temperature of adjusting heat pump unit 2.
When heat-pump apparatus breaks down or when secondary cycle water does not use, enable domestic hot-water's intake pipe 13, control circulating water flow one time by a water circulating pump 8, make recirculated water temperature after high-efficiency condensation heat exchanger 1 reach domestic hot-water's temperature requirement, use as domestic hot-water, the dehydration of a recirculated water supplements by a circulating cooling make-up water pipe 14.
The utility model is based on heat pump principle, a recirculated water with lower temperature utilizes high-efficiency condensation heat exchanger 1 that gas fired-boiler exhaust gas temperature is down to below dew point, absorb obvious heat of smoke and steam gasification latent heat, by source pump 2, a recirculated water is heated to design temperature as low-temperature heat source water by secondary cycle water, the reasonable in design of whole device, ingenious, all parts in device forms an organic whole, all parts acting in conjunction, realize energy recovery efficiency high, energy-saving and emission-reduction, the effect little to the corrosivity of equipment.
In addition, it should be noted that, the specific embodiment described in this description, shape, institute's title of being named etc. of its parts and components can be different, and the above content described in this description is only to the explanation of the utility model structure example.All equivalence variation or simple change of doing according to described structure, feature and the principle of the utility model patent design, are included in the protection domain of the utility model patent.The utility model person of ordinary skill in the field can make various amendments or supplements or adopt similar mode to substitute described specific embodiment; only otherwise depart from structure of the present utility model or surmount this scope as defined in the claims, all should belong to protection domain of the present utility model.
Claims (3)
1. a device that reclaims gas fired-boiler flue gas to condense thermal energy with heat pump mode, comprises high-efficiency condensation heat exchanger, a Heat Exchanger in Circulating Water System outlet, a Heat Exchanger in Circulating Water System inlet tube, smoke inlet pipe and smoke outlet tube, be provided with condensing heat exchanger condensate water discharging mouth in described high-efficiency condensation heat exchanger, smoke inlet, exhanst gas outlet, a recirculated water entrance and a circulating water outlet, one end of described smoke inlet pipe and one end of smoke outlet tube are connected on the smoke inlet and exhanst gas outlet of high-efficiency condensation heat exchanger, one end of one end of a described Heat Exchanger in Circulating Water System outlet and a Heat Exchanger in Circulating Water System inlet tube is connected on a circulating water outlet and a recirculated water entrance of high-efficiency condensation heat exchanger, it is characterized in that: also comprise source pump, a Heat Exchanger in Circulating Water System outlet temperature meter, a circulating water flow meter, a circulating water heating pumping intake piping, a circulating water heating pump discharge pipe, a water circulating pump, a Heat Exchanger in Circulating Water System inlet temperature meter, domestic hot-water's intake pipe, a circulating cooling make-up water pipe, secondary cycle water pump, secondary cycle water return water temperature meter, secondary cycle hydro-thermal pumping intake piping, secondary cycle hydro-thermal pump discharge pipe, secondary cycle water ga(u)ge and secondary cycle hydro-thermal pump discharge thermometer, a described water circulating pump and a Heat Exchanger in Circulating Water System inlet temperature meter are installed on a Heat Exchanger in Circulating Water System inlet tube, and a described Heat Exchanger in Circulating Water System outlet temperature meter and a circulating water flow meter are installed on a Heat Exchanger in Circulating Water System outlet, one end of one end of a described circulating water heating pump discharge pipe and a circulating cooling make-up water pipe is all connected on the other end of a Heat Exchanger in Circulating Water System inlet tube, and one end of one end of a described circulating water heating pumping intake piping and domestic hot-water's intake pipe is all connected on the other end of a Heat Exchanger in Circulating Water System outlet, in described source pump, be provided with recirculated water entrance one time, a circulating water outlet, secondary cycle water inlet and secondary cycle water out, the other end of the other end of a described circulating water heating pumping intake piping and a circulating water heating pump discharge pipe is connected on a recirculated water entrance and a circulating water outlet of source pump, one end of one end of described secondary cycle hydro-thermal pumping intake piping and secondary cycle hydro-thermal pump discharge pipe is connected on the secondary cycle water inlet and secondary cycle water out of source pump, described secondary cycle water pump and secondary cycle water return water temperature meter are installed on secondary cycle hydro-thermal pumping intake piping, described secondary cycle water ga(u)ge and secondary cycle hydro-thermal pump discharge thermometer are installed on secondary cycle hydro-thermal pump discharge pipe.
2. the device that reclaims gas fired-boiler flue gas to condense thermal energy with heat pump mode according to claim 1, is characterized in that: the end heat-exchanging tube bundle along flow of flue gas direction in described high-efficiency condensation heat exchanger adopts corrosion-resistant material.
3. the device that reclaims gas fired-boiler flue gas to condense thermal energy with heat pump mode according to claim 1, is characterized in that: the base plate in described high-efficiency condensation heat exchanger is downward-sloping gradually along flow of flue gas direction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420157019.2U CN203848505U (en) | 2014-04-02 | 2014-04-02 | Device for recovering condensation heat energy of gas boiler flue gas by means of heat pump |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420157019.2U CN203848505U (en) | 2014-04-02 | 2014-04-02 | Device for recovering condensation heat energy of gas boiler flue gas by means of heat pump |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203848505U true CN203848505U (en) | 2014-09-24 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420157019.2U Expired - Lifetime CN203848505U (en) | 2014-04-02 | 2014-04-02 | Device for recovering condensation heat energy of gas boiler flue gas by means of heat pump |
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| CN (1) | CN203848505U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103954039A (en) * | 2014-04-02 | 2014-07-30 | 华电电力科学研究院 | Device and method for recycling smoke condensate heat energy of gas boiler in heat pumping mode |
| WO2018056891A1 (en) * | 2016-09-26 | 2018-03-29 | Flue Gas Recovery Sweden Ab | Flue gas treatment system and method |
| CN107975816A (en) * | 2018-01-03 | 2018-05-01 | 北京龙电宏泰环保科技有限公司 | A kind of method water-saving suitable for gas fired-boiler and gas turbine flue gas depth energy saving |
| CN108488825A (en) * | 2018-05-14 | 2018-09-04 | 江苏康大联合节能科技有限公司 | Nonmetallic flue gas heat-exchange unit preventing freeze in winter system |
-
2014
- 2014-04-02 CN CN201420157019.2U patent/CN203848505U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103954039A (en) * | 2014-04-02 | 2014-07-30 | 华电电力科学研究院 | Device and method for recycling smoke condensate heat energy of gas boiler in heat pumping mode |
| CN103954039B (en) * | 2014-04-02 | 2017-02-08 | 华电电力科学研究院 | Device and method for recycling smoke condensate heat energy of gas boiler in heat pumping mode |
| WO2018056891A1 (en) * | 2016-09-26 | 2018-03-29 | Flue Gas Recovery Sweden Ab | Flue gas treatment system and method |
| CN109564028A (en) * | 2016-09-26 | 2019-04-02 | 瑞典清洁生物热公司 | Flue gas treating system and method |
| CN107975816A (en) * | 2018-01-03 | 2018-05-01 | 北京龙电宏泰环保科技有限公司 | A kind of method water-saving suitable for gas fired-boiler and gas turbine flue gas depth energy saving |
| CN108488825A (en) * | 2018-05-14 | 2018-09-04 | 江苏康大联合节能科技有限公司 | Nonmetallic flue gas heat-exchange unit preventing freeze in winter system |
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