CN205032022U - Ash -laden gas condensation heat recovery and gas cleaning integration system - Google Patents
Ash -laden gas condensation heat recovery and gas cleaning integration system Download PDFInfo
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- CN205032022U CN205032022U CN201520639418.7U CN201520639418U CN205032022U CN 205032022 U CN205032022 U CN 205032022U CN 201520639418 U CN201520639418 U CN 201520639418U CN 205032022 U CN205032022 U CN 205032022U
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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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies for a more efficient combustion or heat usage
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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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
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Abstract
The utility model provides an ash -laden gas condensation heat recovery and gas cleaning integration system, belongs to the heat recovery and the deep purification technical field of ash -laden gas and waste gas. This system includes and adds medicine high flush tank, dividing wall type heat exchanger, falling liquid film condensation absorber and subside the heat exchanger. Dividing wall type heat exchanger is last to be equipped with system's flue gas entry and system's extrinsic cycle water export, and it is continuous with falling liquid film condensation absorber that dividing wall type heat exchanger passes through flue gas line, it arranges below falling liquid film condensation absorber to subside the heat exchanger, the water -locator has been arranged on falling liquid film hole pattern upper portion. The utility model discloses the high -efficient recovery of waste heat, dust removal and the flue gas desulfurization purification etc. Of collecting ash -laden gas and tail gas do not relate to circulating water spray component in an organic whole, need not outside temperature control device, can directly adjust flue gas tail gas wet flue gas desulfurization's optimum condition, have realized the high -efficient falling liquid film desulfurization of flue gas tail gas, have that system operation is reliable, the energy consumption is few, the flue gas flow resistance is little, degree of depth desulfurization and the advantage such as with low costs of removing dust.
Description
Technical field
The utility model relates to a kind of ash-laden gas condense thermal energy and reclaims and gas cleaning integral system, belong to fume afterheat to utilize and deep purifying processing technology field, can be used for energy recovery and the purification of the complicated ingredient flue gas in fire coal, fuel oil heat and power supply boiler and Industrial Boiler flue gas after common mode dedusting.
Background technology
Current fire coal, fuel oil and some gaseous fuels usually contain a large amount of solid particulate matter, SOx and NOx, steam etc. in heat and power supply boiler, Industrial Boiler furnace flue gas, most dust is removed via the technology such as electrostatic precipitation, bag-type dust by solid particulate matter, also have sub-fraction dust not to be removed, need to deepen dedusting.This kind equipment exhaust gas temperature is still higher on the other hand, about 120 ~ 150 DEG C, and in flue gas the content of steam far above the content of steam in ambient atmosphere environment, flue gas is made to contain a large amount of sensible heats and latent heat, if cigarette temperature is significantly reduced to below dew point, can the simultaneously sensible heat of recovered flue gas and latent heat, improve the thermal efficiency of fuel combustion, flue gas condensing also contributes to creating good sulfuric acid and nitric acid condensation removes condition.China's common process of wet desulphurization energy consumption is high, medication mainly with and one of the poor reason of economy be exactly cooling, desulfurizing, and in this process, fume afterheat is not recycled, and its reason has: 1. ash-laden gas condensation can form mud and dirt on heat-transfer surface; 2. high-sulfur flue gas corrosion equipment; 3. flue gas after desulfurization temperature reduces, and waste heat recovery potentiality reduce.Therefore, current ash-laden gas UTILIZATION OF VESIDUAL HEAT IN also mainly concentrates on middle high-temperature flue gas UTILIZATION OF VESIDUAL HEAT IN.Utilizing for this type of low-temperature flue gas of less than 180 DEG C has following three aspect problems to need to solve: 1. efficient, the economic recovery of the fume afterheat degree of depth; 2. the degree of depth udst separation of flue gas; 3. the economical and efficient desulphurization denitration process of flue gas.
To the flue tail gas of gas fired-boiler, published technology mainly adopts dividing wall type heat exchanger that fume afterheat is passed to recirculated water, air or refrigerating medium, as CN204345685U discloses Central Air-Conditioner waste-heat recovery device, the flue tail gas after fuel gas buring and the heat exchange of spiral heat dissipation blade are realized waste heat recovery.CN104456610A, CN104456610A and CN204285583U by heat pump by flue gas waste heat recovery; CN104359314A adopts heat exchanger high-temperature flue gas to add hot-air, CN204372901U discloses the dual-purpose flue gas waste heat recovery apparatus of a machine (flue gas air or water), CN104329974A proposes flue gas waste heat recovery heat pipe-type air-water heat exchanger, and CN102777886A, CN203980639U adopt heat exchanger fume afterheat transmitted by stages feedwater and realize flue gas waste heat recovery; In addition, water is become water smoke by nozzle spray mode by CN101398181A, realizes water smoke and flue gas direct contact heat transfer and carries out waste heat recovery.To the flue tail gas of oil burning boiler, waste heat recovery mainly adopts dividing wall type heat exchanger that fume afterheat is passed to recirculated water.Patent document CN101922702A discloses a kind of flue gas waste heat recovery device for gas-oil boiler and system, adopts soft water heater by flue gas waste heat recovery; Patent document CN201449169U and CN101592444A proposes a kind of wave surface hot plate type energy-saving for combustion gas and smoke of oil-fuel boiler waste heat recovery, utilizes wave surface hot plate type combustion gas and smoke of oil-fuel boiler waste heat of condensation energy recovering economizer by waste heat recovery.In addition, adopt nonmetal replacement metal material can avoid metal erosion problem, conventional metals pipe is replaced to carry out the method for heat exchange as CN201510004641 discloses glass tube, efficiently avoid metal material be subject to flue gas corrosion due to fuel-firing gas-firing tail gas dustiness less, adopt dividing wall type heat exchanger to realize the mode that flue gas and cold side recirculated water or boiler combustion air carry out heating and realize flue gas waste heat recovery.
To fire coal boiler fume tail gas, a kind of scheme still adopts dividing wall type heat exchanger by flue gas waste heat recovery, dividing wall type heat exchanger is metal material or nonmetallic materials, as CN202532512U, CN202432505U and CN102200288A adopt the form of metallic recuperator or heat exchanger tube to realize the waste heat recovery of flue gas.But, a large amount of flue dust can be produced due to during coal fuel combustion, even if after effectively filtering, still more flue dust can be produced in flue gas, produce when needing to consider flue gas cool-down in condensed water containing flue dust, as CN104676619A discloses a kind of gas fired-boiler chimney and the two-in-one device of fountain flue gas waste heat recovery assembly, multilayer is resistant to elevated temperatures revolves in louvered stainless steel helices to adopt nozzle spray mode to be sprayed at by cooling water, thus realizes flue gas waste heat recovery.CN201216155824.9 utilize spray mode by flue gas waste heat recovery, patent document (CN201410397374) select spray assemblies by Water spray to the filler of bigger serface and and smoke contact heat exchange.But, when shower water absorbs heat, seldom consider and cause nozzles spray to lose efficacy and long-term corrosion problem because plug nozzle and outside flue dust condense near nozzle containing flue dust in water, for this problem, Chinese patent literature (CN201320198802) is then provided with rinse spray device, and the basis of original spray design adds Periodic scale removal measure.Larger power consumption or the easy regular blocking of nozzle is all needed in above-mentioned spraying or rinse spray device.
In addition, Chinese patent literature (CN102407070A) discloses the device of a kind of falling film type flue tail gas waste heat recovery, effectively can take into account gas purification, to oil-burning gas-fired boiler using waste heat from tail gas reclaim and purified treatment better, but in the waste heat recovery and purified treatment of SOx and the higher coal-fired flue-gas of smoke content or waste gas still Shortcomings, now moisture film wet absorption sulfur removal technology needs more desulfurization medicament, simultaneously, dividing wall type heat exchanger is directly embedded in bottom settling tank, space needed for precipitation buffering must be obtained by increasing device height when smoke sludge is more, in addition, the method of the direct falling film absorption smoke heat energy of this technology, evaporate in the flue tail gas of high temperature low humidity with making water section, cause high-grade energy recovery weak effect.
In sum, prior art is only confined to the prior art combination to flue gas heat recovery and desulphurization denitration, and for the larger flue tail gas waste heat recovery of dustiness, still need a kind of integrated treatment scheme taking into account efficient waste heat recovery, flue gas deep purifying, need to take into account system cloud gray model low power capabilities simultaneously.
Utility model content
The purpose of this utility model is to provide and waits ash-laden gas and the energy recovery of waste gas and the integral system of purification in field in coal-burning boiler and industry, to realizing the target of the degree of depth dedusting of ash-laden gas, High Efficiency Thermal recovery and cleaning and desulfurization.
The technical solution of the utility model is as follows:
A kind of ash-laden gas condense thermal energy reclaims and gas cleaning integral system, and it is characterized in that, this system comprises dosing elevated tank, dividing wall type heat exchanger, at least one-level down-film condenser absorber and sedimentation heat exchanger; Described dividing wall type heat exchanger is provided with system smoke inlet and system outer circulation water out, and dividing wall type heat exchanger is connected with down-film condenser absorber by flue gas pipeline; Described sedimentation heat exchanger is arranged in below down-film condenser absorber; Arrange smoke distributor, multiple falling liquid film hole pattern, water fender and system exhanst gas outlet successively along flue gas flow direction in every grade of down-film condenser absorber, be furnished with water-locator on falling liquid film hole pattern top; Described dosing elevated tank is arranged in the top of water-locator; Described sedimentation heat exchanger contains settling module, external coil pipe module, pool coil pipe module and recirculated water water supply module; Described external coil pipe module arrangement is in the bottom of settling module, and the outside wall surface of external coil pipe module is provided with embedded spiral coil, and external coil pipe module is furnished with system sewage draining exit and system outer circulation water inlet; The sewage draining exit of dividing wall type heat exchanger and the discharge outlet of down-film condenser absorber are connected with described settling module respectively by pipeline; Periodical feeding module is connected with dosing elevated tank with pipeline by water circulating pump.
Another technical characteristic of the present utility model is: described dividing wall type heat exchanger is arranged along flow of flue gas direction, and with the angle of horizontal plane 5 ° ~ 25 °.
Preferably, in technique scheme, described smoke distributor adopts drainage plate structure.
Preferably, in technique scheme, in described multiple falling liquid film hole pattern, the spacing range of adjacent two falling liquid film hole patterns is 0.5 ~ 10cm, mesh on falling liquid film hole pattern is uniform diamond structure, and two acute angles of rhombus are arranged in vertical direction, and two obtuse angles of rhombus are arranged in horizontal direction.
The utility model is relative with prior art, has the following advantages and beneficial effect: 1. for ash-laden gas tail gas or waste vapour, realizes the integrated technique of collection falling film condensation heat exchange, falling film absorption flue dust and falling liquid film desulfurization; 2. compared with fountain device, the utility model does not relate to recirculated water sprinkler part, therefore there is not nozzle because spraying and frequent jams problem for a long time; 3., when adopting two-stage or multi-stage falling-film condensation absorber, the outer circulation water of higher temperature can be produced; 4., compared with existing fountain heat recovery technology, recovery stage by stage and the utilization of obvious heat of smoke and latent heat is realized cost-effectively; 5. the utility model is without the need to external temperature control device, and flue tail gas is directly adjusted to the optimum condition of wet desulphurization by heat recovery heat exchanger, achieves the high-efficiency falling film desulfurization of flue tail gas; 6. the heat contained in mud can fully reclaim by external coil heat exchange module of the present utility model; 7., compared with conventional porous filler, the utility model adopts falling liquid film hole pattern group structure, and the flue gas of proposition directly crosses the falling liquid film hole pattern prescription case of band moisture film, achieves water and fully contacts with flue gas and be conducive to heat and mass transfer enhancement and desulfurization.
Accompanying drawing explanation
Fig. 1 is that a kind of ash-laden gas condense thermal energy of the present utility model reclaims the principle schematic with gas cleaning integral system.
Fig. 2 is one of the present utility model external coil pipe modular structure schematic diagram.
Fig. 3 is embedded spiral coil structural representation of the present utility model.
Fig. 4 is the structural representation of a kind of falling liquid film hole pattern of the present utility model.
In figure: 1-system smoke inlet; 2-dividing wall type heat exchanger; The exhanst gas outlet of 3-dividing wall type heat exchanger; The recirculated water entrance of 4-dividing wall type heat exchanger; 5-system outer circulation water out; The sewage draining exit of 6-dividing wall type heat exchanger; 7-down-film condenser absorber; 8-smoke distributor; 9-falling liquid film hole pattern group; 10-water-locator; 11-dosing elevated tank; 12-water fender; 13-system exhanst gas outlet; The discharge outlet of 14-down-film condenser absorber; The Inner eycle water inlet of 15-sedimentation heat exchanger; 16-sedimentation heat exchanger; 17-settling module; The external coil pipe module of 18-; 19-system sewage draining exit; 20-system outer circulation water inlet; 21-water circulating pump; 22-recirculated water water supply module; 23-pool coil pipe module; The coil outlets of 24-pool coil pipe module; The embedded spiral coil delivery port of 25-; 26-mud; The embedded spiral coil of 27-.
Detailed description of the invention
Below in conjunction with accompanying drawing, system architecture of the present utility model and the course of work are described further.
Fig. 1 is that a kind of ash-laden gas condense thermal energy of the present utility model reclaims the principle schematic with gas cleaning integral system, and this system comprises dosing elevated tank 11, dividing wall type heat exchanger 2, at least one-level down-film condenser absorber 7 and sedimentation heat exchanger 16; Described dividing wall type heat exchanger 2 is provided with system smoke inlet 1 and system outer circulation water out 5, and dividing wall type heat exchanger is connected with down-film condenser absorber 7 by flue gas pipeline; Described sedimentation heat exchanger 16 is arranged in below down-film condenser absorber 7; Arrange smoke distributor 8, multiple falling liquid film hole pattern 9, water fender 12 and system exhanst gas outlet 13 successively along flue gas flow direction in every grade of down-film condenser absorber 7, be furnished with water-locator 10 on falling liquid film hole pattern 9 top; Described dosing elevated tank 11 is arranged in the top of water-locator 10; Described sedimentation heat exchanger 16 is containing settling module 17, external coil pipe module 18, pool coil pipe module 23 and recirculated water water supply module 22; Described external coil pipe module 18 is arranged in the bottom of settling module 17, the outside wall surface of external coil pipe module 18 is provided with embedded spiral coil 27, and external coil pipe module is furnished with system sewage draining exit 19 and system outer circulation water inlet 20 (see Fig. 2); The sewage draining exit 6 of dividing wall type heat exchanger and the discharge outlet 14 of down-film condenser absorber 7 are connected with described settling module 17 respectively by pipeline; Periodical feeding module 22 is connected with dosing elevated tank 11 with pipeline by water circulating pump 21; Outer circulation water in described embedded spiral coil carries out heat exchange with the mud from settling module 17; Described dividing wall type heat exchanger 2 is arranged along flow of flue gas direction, and with the angle of horizontal plane 5 ° ~ 25 °; Described smoke distributor 8 adopts drainage plate structure.
Fig. 2 is one of the present utility model external coil pipe modular structure schematic diagram.Outer circulation water flows in the embedded spiral coil 27 of external coil pipe module 18 from system outer circulation water inlet 20, heat exchange is carried out at embedded spiral coil internal and external circulating water and the mud from settling module 17, discharge from system sewage draining exit 19 after mud is cooled to 45-75 DEG C, outer circulation water flows to pool coil pipe module 23 from embedded spiral coil water outlet pipeline after heating up; Spiral coil wherein in external coil pipe module 18 is embedded in the outside wall surface of module, and module outside wall surface forms helical structure.Fig. 3 is spiral coil structural representation of the present utility model, and this embedded mode is conducive to the heat exchange between coil pipe and mud.
Fig. 4 is the structural representation of a kind of falling liquid film hole pattern of the present utility model, in multiple falling liquid film hole pattern 9, the spacing range of adjacent two falling liquid film hole patterns is 0.5 ~ 10cm, mesh on falling liquid film hole pattern is uniform diamond structure, two acute angles of rhombus are arranged in vertical direction, and two obtuse angles of rhombus are arranged in horizontal direction.
The course of work of the present utility model and principle as follows:
Flue tail gas enters dividing wall type heat exchanger 2 by system smoke inlet 1 and carries out heat exchange with the outer circulation water from sedimentation heat exchanger 16, then enter in down-film condenser absorber 7, in down-film condenser absorber 7, flue gas carries out reorganization air-flow through smoke distributor 8, water is sent in dosing elevated tank 11 by water circulating pump 21 by recirculated water water supply module 22, in dosing elevated tank 11, water relies on gravity to flow in water-locator 10 through pipeline after fully mixing with desulfurization medicament, water is evenly distributed on multiple falling liquid film hole pattern 9 by water-locator, and water forms subcooled water film on falling liquid film hole pattern under gravity, when penetrating falling liquid film hole pattern from the flue gas in dividing wall type heat exchanger 2, flue gas and subcooled water film carry out heat and mass, then the flue gas of lower temperature is discharged from system exhanst gas outlet 13 via water fender 12, achieves heat exchange between flue gas and water and water to the purified treatment of flue gas, outer circulation water enters in the embedded spiral coil 27 of external coil pipe module 18 from outer circulation water inlet 20, to discharge from the discharge outlet 14 of down-film condenser absorber containing the sewage of flue dust and flow into through pipeline the settling module 17 of sedimentation heat exchanger 16, sewage is separated into clear water and mud by settling module 17, mud carries out indirect heat exchange with the outer circulation water in embedded spiral coil in external coil pipe module 18, mud temperature is discharged from sewage draining exit 19 after reducing, clear water then enters in pool coil pipe module 23 with the form of overflow, in pool coil pipe module, clear water carries out indirect heat exchange with the outer circulation water from external coil pipe module 18, flow into after clear water temperature reduces in recirculated water water supply module 22, achieve a circulation of Inner eycle water, realize after outer circulation water and mud carry out heat exchange being warming up to 35-55 DEG C for the first time, then outer circulation water realizes second time after flowing into and carrying out heat exchange with clear water in pool coil pipe module 23 and is warming up to 45-65 DEG C, last outer circulation water realizes after flowing into and carrying out heat exchange with flue gas in dividing wall type heat exchanger 2 being warming up to more than 70 DEG C for the third time, then the outer circulation water of higher temperature flows out via the outer circulation water out 5 of system, realizes heat supply to external world.
For dust-laden, containing the higher flue gas of sulfur, can by increasing the technical scheme of falling liquid film hole pattern quantity, also by the concrete form of connect again a set of down-film condenser absorber and supporting dosing elevated tank etc., adopt two-stage down-film condenser absorber technology scheme, still can realize the energy recovery of flue gas and dedusting, purification efficiently.
In the fields such as coal-burning boiler and industry, after dust removal process is carried out to the flue gas (or waste gas) of dust-laden, a small amount of molecule flue dust is still had to discharge along with flue tail gas, in the dedusting of the flue tail gas degree of depth, the greatest problem that existing fountain dedusting method faces is: technically, recirculated water forms droplet (or little droplet) in the mode of jet spray on shower nozzle, should be enough little in order to form droplet shower nozzle aperture, so at recirculated water self containing a small amount of mud and shower nozzle outward containing under the flue tail gas long term of flue dust, easily there is blocking and lose spray ability in shower nozzle aperture, say that jet spray forms the process of droplet by pump power consumption larger for needs from economy, the longtime running of equipment costly.Adopt the organization plan of water-locator and falling liquid film hole pattern for this reason in system of the present utility model, correspondingly select and form moisture film but not spray droplet and flue gas and interact.The water distribution principle of water-locator is that water is assigned in falling liquid film hole pattern group with the principle of water overflow under the effect of gravitional force, the falling liquid film hole pattern prescription case of vertically arranging is have selected in system of the present utility model, therefore when water is assigned on hole pattern equably at top, control the water yield enough little to such an extent as to avoid hole pattern formed cascade, the technical scheme that rhombus acute angle arranges up and down is proposed according to the diamond structure feature of hole pattern, in water certain root netting twine trickling process along hole pattern, when running into next diamond structure, water is at gravity, under the acting in conjunction of surface tension and self inertial flow, can separate from two acute angles of next diamond structure and shunt along netting twine, when the hole pattern of multiple diamond structure so flows, achieve moisture film cover the netting twine of hole pattern preferably and don't can diamond structure be blocked, define the falling liquid film process along hole pattern netting twine, moisture film is not directly trickle along gravity direction in the process of trickling downwards simultaneously, but trickle along netting twine, the liquid form of this moisture film adds the time of contact of water and flue tail gas, be conducive to dedusting, heat exchange and desulfurization.
Because flue tail gas is through each falling liquid film hole pattern, air-flow is reorganized the rear aperture through hole pattern, then air-flow enters next falling liquid film hole pattern group after having mixing again, achieve flue gas and the moisture film on netting twine fully contact realize moisture film to flue gas condensing, absorb flue dust and absorb the effect of SOx, the resistance absorbed in the falling film of SOx and flue dust is in fume side, so air-flow is through the reorganization of multilayer aperture with after absorbing again, the clean-up effect of flue gas is better; After water absorbs SOx, desulfurization medicament (as NaON, CaO etc.) in SOx and water interacts, eliminate the acidity being unfavorable for flue gas desulfurization, owing to constantly absorbing flue dust and SOx, drop down at current and become sewage to during down-film condenser absorber bottom, sewage is introduced in sedimentation heat-exchanger rig or small-sized settling tank and carry out sludge settling, because heat that mud is with is more, therefore make mud and outer circulation water carry out heat exchange lower the temperature after discharge, the mud of discharge can as raw materials of industry such as chemical fertilizer.
In addition, dividing wall type heat exchanger has been selected to carry out elementary cooling to flue gas and do not adopt direct falling liquid film or spray process to carry out waste heat recovery in the utility model, main cause is that the relative humidity in the low-temperature flue gas tail gas of higher temperature is very low, if allow flue tail gas directly contact with water, water must be caused to absorb heat evaporate, total enthalpy in flue tail gas is not changed substantially, but in flue gas, the sensible heat thermal energy of higher temperature is in order to the latent heat energy of relatively lower temp, and the recycle value reclaiming the heat energy of lower temperature is lower.And after adopting dividing wall type heat exchanger, the sensible heat heat energy of the most higher temperatures in flue tail gas can be recovered effectively, the mode so arranging indirect heat exchange and direct heat transfer series connection achieves the staged recovery of flue tail gas heat energy, simultaneously because SOx concentration in coal-fired flue-gas tail gas is higher, the SOx of higher concentration condenses by dividing wall type heat exchanger and absorbs and directly enter in sedimentation heat-exchanger rig, avoid moisture film and need more desulfurization medicament because absorbing excessive SOx, significantly reduce desulphurization cost.
Claims (4)
1. an ash-laden gas condense thermal energy reclaims and gas cleaning integral system, it is characterized in that, this system comprises dosing elevated tank (11), dividing wall type heat exchanger (2), at least one-level down-film condenser absorber (7) and sedimentation heat exchanger (16); Described dividing wall type heat exchanger (2) is provided with system smoke inlet (1) and system outer circulation water out (5), and dividing wall type heat exchanger is connected with down-film condenser absorber (7) by flue gas pipeline; Described sedimentation heat exchanger (16) is arranged in below down-film condenser absorber (7); Arrange smoke distributor (8), multiple falling liquid film hole pattern (9), water fender (12) and system exhanst gas outlet (13) successively along flue gas flow direction in every grade of down-film condenser absorber (7), be furnished with water-locator (10) on falling liquid film hole pattern (9) top; Described dosing elevated tank (11) is arranged in the top of water-locator (10); Described sedimentation heat exchanger (16) is containing settling module (17), external coil pipe module (18), pool coil pipe module (23) and recirculated water water supply module (22); Described external coil pipe module (18) is arranged in the bottom of settling module (17), the outside wall surface of external coil pipe module (18) is provided with embedded spiral coil (27), and external coil pipe module is furnished with system sewage draining exit (19) and system outer circulation water inlet (20); The sewage draining exit (6) of dividing wall type heat exchanger (2) and the discharge outlet (14) of down-film condenser absorber (7) are connected with described settling module (17) respectively by pipeline; Periodical feeding module (22) is connected with dosing elevated tank (11) with pipeline by water circulating pump (21).
2. a kind of ash-laden gas condense thermal energy according to claim 1 reclaims and gas cleaning integral system, it is characterized in that: described dividing wall type heat exchanger (2) is arranged along flow of flue gas direction, and with the angle of horizontal plane 5 ° ~ 25 °.
3. a kind of ash-laden gas condense thermal energy according to claim 1 reclaims and gas cleaning integral system, it is characterized in that: described smoke distributor (8) adopts drainage plate structure.
4. a kind of ash-laden gas condense thermal energy according to claim 1,2 or 3 reclaims and gas cleaning integral system, it is characterized in that: in described multiple falling liquid film hole pattern (9), the spacing range of adjacent two falling liquid film hole patterns is 0.5 ~ 10cm, mesh on falling liquid film hole pattern is uniform diamond structure, two acute angles of rhombus are arranged in vertical direction, and two obtuse angles of rhombus are arranged in horizontal direction.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520639418.7U CN205032022U (en) | 2015-08-21 | 2015-08-21 | Ash -laden gas condensation heat recovery and gas cleaning integration system |
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| CN201520639418.7U CN205032022U (en) | 2015-08-21 | 2015-08-21 | Ash -laden gas condensation heat recovery and gas cleaning integration system |
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| CN205032022U true CN205032022U (en) | 2016-02-17 |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105080245A (en) * | 2015-08-21 | 2015-11-25 | 北京建筑大学 | System and method for integrally recycling condensation heat energy of flue gas with dust and purifying flue gas |
| CN105688778A (en) * | 2016-03-29 | 2016-06-22 | 常州市先导干燥设备有限公司 | Closed-cycle high-temperature airflow reaction device |
| CN107158853A (en) * | 2017-07-07 | 2017-09-15 | 贵州南风日化有限公司 | A kind of washing powder spray drying tower tail gas dust cleaning apparatus |
| CN111486464A (en) * | 2020-03-25 | 2020-08-04 | 清华大学 | Waste heat method pollutant recycling-based waste-free garbage power plant process mode and system |
| CN112128791A (en) * | 2020-09-14 | 2020-12-25 | 张斯瑞 | Deep waste heat recovery method for smoke discharge of gas-fired boiler |
| CN113669780A (en) * | 2021-09-06 | 2021-11-19 | 周增有 | Environment-friendly heat supply system |
-
2015
- 2015-08-21 CN CN201520639418.7U patent/CN205032022U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105080245A (en) * | 2015-08-21 | 2015-11-25 | 北京建筑大学 | System and method for integrally recycling condensation heat energy of flue gas with dust and purifying flue gas |
| CN105688778A (en) * | 2016-03-29 | 2016-06-22 | 常州市先导干燥设备有限公司 | Closed-cycle high-temperature airflow reaction device |
| CN107158853A (en) * | 2017-07-07 | 2017-09-15 | 贵州南风日化有限公司 | A kind of washing powder spray drying tower tail gas dust cleaning apparatus |
| CN111486464A (en) * | 2020-03-25 | 2020-08-04 | 清华大学 | Waste heat method pollutant recycling-based waste-free garbage power plant process mode and system |
| CN111486464B (en) * | 2020-03-25 | 2024-04-26 | 清华大学 | Waste-free garbage power plant process mode and system based on waste heat method pollutant reclamation |
| CN112128791A (en) * | 2020-09-14 | 2020-12-25 | 张斯瑞 | Deep waste heat recovery method for smoke discharge of gas-fired boiler |
| CN113669780A (en) * | 2021-09-06 | 2021-11-19 | 周增有 | Environment-friendly heat supply system |
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