CN204629542U - Gas cleaning and waste heat recovery heating plant - Google Patents
Gas cleaning and waste heat recovery heating plant Download PDFInfo
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- CN204629542U CN204629542U CN201520298854.2U CN201520298854U CN204629542U CN 204629542 U CN204629542 U CN 204629542U CN 201520298854 U CN201520298854 U CN 201520298854U CN 204629542 U CN204629542 U CN 204629542U
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- cooling water
- flue gas
- pipe
- heat
- heat recovery
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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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Abstract
The utility model discloses a kind of gas cleaning and waste heat recovery heating plant, comprise direct contact type waste-heat recoverer and circulation, it is characterized in that: direct contact type waste-heat recoverer comprises bubbler, smoke-intake pipe, overflow pipe, cylinder, bubbling segment, spray section, spray thrower, water inlet pipe, demister and smoke exhaust pipe; High-temperature flue gas enters cooling water in the form of bubbles through bubbler, carries out the exchange of direct contact type caloic at bubbling segment; The flue gas of emerging from cooling water enters spray section, and the cooling water sprayed with spray thrower is direct contact heat transfer mass transfer again; Cooling water after heat absorption enters circulation, by the heat exchanger heating heating agent in circulation, thus outward supplying heat; Purification and the flue gas after lowering the temperature are discharged from the smoke exhaust pipe on cylinder top.The utility model adopts flue gas and cooling water two-part direct contact heat transfer mass transfer, makes flue gas obtain fully cooling and purify completely, is applicable to gas cleaning and the waste heat recovery of all combustion gas Thermal Equipments.
Description
Technical field
This use is novel relates to a kind of flue gas waste heat recovery apparatus, particularly a kind of gas cleaning for combustion gas Thermal Equipment and waste heat recovery heating plant.
Technical background
Along with the fast development of China's economy, energy-output ratio increases day by day, and air quality also goes from bad to worse simultaneously.Require the today constantly promoted at energy-saving, emission-reducing, environment friendly, natural gas is as clean and that calorific value the is higher energy, and in China's urban energy consumption structure, constant rises.At present, major part coal-burning boiler in China large-and-medium size cities changes gas fired-boiler into.For most gas fired-boiler, its exhaust gas temperature still more than 150 DEG C, even up to 250 DEG C.In gas fired-boiler flue gas, containing water vapor is about 18%(percent by volume), there is a large amount of obvious heat of smoke and steam latent heat, flue gas brings a large amount of heats into ambient air, not only wastes mass energy, boiler thermal output is reduced, and pollutes environment.Usual at boiler tail clipping room wall type heat recovery heat exchanger (as fin tube type energy-saving appliance) at present, can only part sensible heat in recovered flue gas, and waste heat recovery efficiency is lower, and the flow resistance of flue gas is comparatively large, causes larger back pressure to boiler.In flue gas, the dew point of steam is about about 57 DEG C, if exhaust gas temperature can be down to below steam dew point, realizes the abundant recycling of fume afterheat, boiler efficiency will be increased substantially, boiler oil consumption can be reduced simultaneously, reduce acid gas emissions, and recyclable part water resource.
Existing direct contact type flue gas waste heat recovery apparatus does not have bubble type, only adopt simple spray, or adopt simple herringbone water fender, make flue gas and shower water can not abundant contact heat-exchanging, also the employing filler had is to increase the contact area of flue gas and cooling water, but the flow resistance of flue gas is comparatively large, and interpolation filler easily produces wall flow phenomenon.In addition, cool water shower device and gas approach structure are simple, are difficult to realize cooling water and flue gas is uniformly distributed in cylindrical shell, thus reduce the heat and mass efficiency between cooling water and flue gas.
Summary of the invention
This uses novel object to be the defect overcoming above-mentioned prior art, a kind of gas cleaning efficiently and waste heat recovery heating plant are provided, solve the technical problems such as the waste heat recovery efficiency that existing waste-heat recoverer exists is low, gas cleaning weak effect, flow resistance are large.
This uses the following technical scheme of novel employing: provide a kind of gas cleaning and waste heat recovery heating plant, comprise direct contact type waste-heat recoverer and circulation, direct contact type waste-heat recoverer comprises bubbler, smoke-intake pipe, overflow pipe, cylinder, bubbling segment, spray section, spray thrower, water inlet pipe, demister and smoke exhaust pipe; High-temperature flue gas enters cooling water in the form of bubbles through bubbler, carries out the exchange of direct contact type caloic at bubbling segment; The flue gas of emerging from cooling water enters spray section, and the cooling water sprayed with spray thrower is direct contact heat transfer mass transfer again; Cooling water after heat absorption enters circulation, by the heat exchanger heating heating agent in circulation, thus outward supplying heat; Purification and the flue gas after lowering the temperature are discharged from the smoke exhaust pipe on cylinder top.
Arrange demister between described flue gas exhaust pipe and spray thrower, demister adopts multilayer corrugated plate to be folded into grid-like.
Described spray thrower adopts the concentric coil pipe that upper welding two calibers of water inlet supervisor are less, and coil pipe is horizontally disposed, and its bottom interval 60o installs a nozzle, and according to the space size of actual spray section, spray thrower can arrange one deck or two-layer.
Described bubbling segment and spray section are the heat and mass spaces of flue gas and cooling water, and bubbling segment fills cooling water, and bubbler is immersed in cooling water, and spray section is cavity.
Described bubbler adopts the upper concentric coil pipe of welding two to three of flue gas air inlet supervisor, and coil pipe is horizontally disposed, and its bottom interval is about 20mm and gets out the exhaust smoke hole that diameter is 4-8mm.
Described circulation comprises stop valve, filter, PH value detector, electric check valve, lye tank, circulating pump, heat exchanger, moisturizing stop valve, filling pipe and connecting pipe, PH value detector detects the pH value of cooling water automatically, and automatically regulates the pH value of cooling water by electric check valve filling alkali lye.
Described heat exchanger adopts sub-thread stream wrap-round tubular heat exchanger, and hot water walks tube side, and heating agent walks shell side.
The operation principle of gas cleaning and waste heat recovery heating plant is as follows: cooling water enters spray thrower through water inlet pipe, is evenly sprayed downwards, and flow from top to bottom by the shower nozzle of spray thrower; High-temperature flue gas enters bubbler through smoke-intake pipe, is entered in the form of bubbles in bubbling segment cooling water, and flow from bottom to top by bubbler; Two media forms adverse current in cylinder, and high-temperature flue gas contacts with cooling water first in the form of bubbles, carries out direct contact type heat and mass, and the dust comprised in the part latent heat of this stage flue gas and sensible heat and flue gas and sour gas are only absorbed by the water; The flue gas of emerging from bubbling segment enters spray section, and the water that flue gas and spray thrower spray carries out secondary transmission of heat by contact mass transfer, is fully absorbed at this stage flue gas remainder latent heat and sensible heat and other impurity; Flue gas through twice caloic exchange enters demister, and got rid of by smoke exhaust pipe after demister dehydration, demister is also the process once preventing moisture and heat loss to the dehydration of flue gas; Cooling water, after spray section and bubbling segment absorb the heat in flue gas for twice, enters circulation, by the heat exchanger heating heating agent in circulation, thus outward supplying heat, cooling water again enters spray thrower and recycles.In flue gas, absorbed impurity is regularly discharged by the blow-off pipe of cylinder bottom.
After this uses novel employing technique scheme, compared with prior art there is following beneficial effect: adopt coiled spray thrower that cooling water can be made to be evenly distributed in cylinder, be conducive to fully contacting with flue gas; Adopt spray section and bubbling segment two-part heat and mass, larger in the specific area of spray section water, abundant and less to the resistance of flue gas with smoke contacts, enter in the form of bubbles in cooling water at bubbling segment high-temperature flue gas, become the heat and mass surface of gas-liquid contact, considerably increase the contact area of flue gas and cooling water, be more conducive to the heat and mass of flue gas and cooling water, and two-part heat and mass is had complementary advantages; Bubbler adopts coiled distributor, distributes more even after making flue gas enter cylinder; Flue gas and cooling water be complete adverse current in cylinder, be conducive to the motive force increasing heat and mass, the sensible heat in cooling water energy efficient absorption flue gas and latent heat, improve heat transfer efficiency greatly, simultaneously also can sour gas in efficient absorption flue gas and dust, flue gas is purified completely.
Flue gas is after gas cleaning and waste heat recovery heating plant, and exhaust gas temperature can be reduced to about 35 DEG C, and the thermal efficiency of boiler can improve about 10%.Compact conformation, the heat and mass efficiency of gas cleaning and waste heat recovery heating plant are higher, normal pressure run, safe and reliable, be applicable to gas cleaning and the waste heat recovery of all combustion gas Thermal Equipments.
Accompanying drawing explanation
Fig. 1 is the structural representation of gas cleaning and waste heat recovery heating plant;
Fig. 2 is the structural representation of spray thrower;
Fig. 3 is the structural representation of bubbler.
Reference numeral, 1-smoke exhaust pipe; 2-demister; 3-spray thrower; 4-cylinder; 5-spray section; 6-smoke-intake pipe; 7-bubbling segment; 8-bubbler; 9-overflow pipe; 10-blow-off pipe; 11-supporting leg; 12-stop valve; 13-filter; 14-PH value detector; 15-electric check valve; 16-lye tank; 17-circulating pump; 18-heat exchanger; 19-filling pipe; 20-moisturizing stop valve; 21-water inlet pipe.
Detailed description of the invention
The detailed description of the invention of gas cleaning and waste heat recovery heating plant is further illustrated below in conjunction with accompanying drawing.
As shown in Figure 1, gas cleaning and waste heat recovery heating plant comprise contact waste-heat recoverer and circulation, first cylinder is welded with the conical head of lower end, then bubbler, smoke-intake pipe, overflow pipe, water inlet pipe, spray thrower, demister, smoke exhaust pipe are arranged in cylinder from bottom to up successively, then the upper end of cylinder adopts Flange joint ellipsoidal head.
Bubbler adopts the upper concentric coil pipe of welding two to three of flue gas air inlet supervisor, and coil pipe is horizontally disposed, and its bottom interval is about 20mm and gets out the exhaust smoke hole that diameter is 4-8mm.Bubbler is connected with the smoke-intake pipe being positioned at cylinder bottom, and bubbler is heavy invades in water.Blow-off pipe is installed on the bottom conical head of cylinder.
Part below the bottom cooling water surface of cylinder is bubbling segment, installs overflow pipe, prevent the too high refluence smoke-intake pipe of the water surface in cylinder in bubbling segment; The space cooled between more than the water surface to spray thrower is spray section, and spray section is cavity, and its height is determined according to the flue gas flow of reality and cool water shower amount.
Spray thrower adopts the concentric coil pipe that upper welding two calibers of water inlet supervisor are less, coil pipe is horizontally disposed, and its bottom interval 60o installs a nozzle, and spray thrower water inlet supervisor is connected with the cooling water inlet pipe being positioned at cylindrical shell top, as far as possible near the demister on top, so that overall structure is compacter.According to the space size of spray section, spray thrower can arrange one deck or two-layer, to improve spraying effect.
Smoke exhaust pipe is installed on the ellipsoidal head of cylinder upper end, arranges demister between smoke exhaust pipe and spray thrower, and demister adopts multilayer corrugated plate to be folded into grid-like, and as far as possible near smoke exhaust pipe.
Stop valve, filter, PH value detector, electric check valve, lye tank, circulating pump, heat exchanger are connected by pipeline and form circulation, and is connected with the outlet pipe of cylinder, water inlet pipe and filling pipe.
The foregoing is only this and use novel preferred embodiment; not novel in order to limit this use; allly use within novel spirit and principle at this, any amendment done, equivalent replacement, improvement etc., all should be included in this and use within novel protection domain.
Claims (7)
1. a gas cleaning and waste heat recovery heating plant, comprise direct contact type waste-heat recoverer and circulation, it is characterized in that: direct contact type waste-heat recoverer comprises bubbler, smoke-intake pipe, overflow pipe, cylinder, bubbling segment, spray section, spray thrower, water inlet pipe, demister and smoke exhaust pipe; High-temperature flue gas enters cooling water in the form of bubbles through bubbler, carries out the exchange of direct contact type caloic at bubbling segment; The flue gas of emerging from cooling water enters spray section, and the cooling water sprayed with spray thrower is direct contact heat transfer mass transfer again; Cooling water after heat absorption enters circulation, by the heat exchanger heating heating agent in circulation, thus outward supplying heat; Purification and the flue gas after lowering the temperature are discharged from the smoke exhaust pipe on cylinder top.
2. gas cleaning according to claim 1 and waste heat recovery heating plant, is characterized in that, described bubbling segment and spray section are the heat and mass spaces of flue gas and cooling water, and bubbling segment fills cooling water, and bubbler is immersed in cooling water, and spray section is cavity.
3. gas cleaning according to claim 1 and waste heat recovery heating plant, it is characterized in that, described bubbler adopts the upper concentric coil pipe of welding two to three of flue gas air inlet supervisor, and coil pipe is horizontally disposed, and its bottom interval is about 20mm and gets out the exhaust smoke hole that diameter is 4-8mm.
4. gas cleaning according to claim 1 and waste heat recovery heating plant, it is characterized in that, described spray thrower adopts the concentric coil pipe that upper welding two calibers of water inlet supervisor are less, coil pipe is horizontally disposed, its bottom interval 60o installs a nozzle, according to the space size of actual spray section, spray thrower can arrange one deck or two-layer.
5. gas cleaning according to claim 1 and waste heat recovery heating plant, is characterized in that, arranges demister between described smoke exhaust pipe and spray thrower, and demister adopts multilayer corrugated plate to be folded into grid-like.
6. gas cleaning according to claim 1 and waste heat recovery heating plant, it is characterized in that, described circulation comprises stop valve, filter, PH value detector, electric check valve, lye tank, circulating pump, heat exchanger, moisturizing stop valve, filling pipe and connecting pipe, described PH value detector detects the pH value of cooling water automatically, and automatically regulates the pH value of cooling water by electric check valve filling alkali lye.
7. gas cleaning according to claim 1 and waste heat recovery heating plant, is characterized in that, described heat exchanger adopts sub-thread stream wrap-round tubular heat exchanger, and hot water walks tube side, and heating agent walks shell side.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520298854.2U CN204629542U (en) | 2015-05-11 | 2015-05-11 | Gas cleaning and waste heat recovery heating plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520298854.2U CN204629542U (en) | 2015-05-11 | 2015-05-11 | Gas cleaning and waste heat recovery heating plant |
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| CN204629542U true CN204629542U (en) | 2015-09-09 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520298854.2U Expired - Fee Related CN204629542U (en) | 2015-05-11 | 2015-05-11 | Gas cleaning and waste heat recovery heating plant |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104791823A (en) * | 2015-05-11 | 2015-07-22 | 郑州大学 | Heat supplying device for smoke purification and waste heat recovery |
| CN106123313A (en) * | 2016-06-27 | 2016-11-16 | 无锡锡能锅炉有限公司 | A kind of gas fired-boiler heat transmission equipment |
| CN107013896A (en) * | 2017-04-10 | 2017-08-04 | 苏州庆丰包装材料有限公司 | For the steam supply system in production |
| CN107478070A (en) * | 2017-09-24 | 2017-12-15 | 贵州电力设计研究院 | A kind of fountain flue gas water- to-water heat exchanger for generating set |
| CN107990744A (en) * | 2017-12-08 | 2018-05-04 | 佘峰 | A kind of high smelting furnace fume extractor of heat utilization efficiency |
| CN108870427A (en) * | 2018-09-10 | 2018-11-23 | 甘肃红峰机械有限责任公司 | A kind of fume waste heat recyclable device |
| CN109224721A (en) * | 2018-11-21 | 2019-01-18 | 吴迎莉 | A kind of flue gas scrubbing apparatus and method for washing flue gas |
| CN111678354A (en) * | 2020-05-21 | 2020-09-18 | 四川省简阳空冷器制造有限公司 | Method for indirectly cooling air through conversion gas |
-
2015
- 2015-05-11 CN CN201520298854.2U patent/CN204629542U/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104791823A (en) * | 2015-05-11 | 2015-07-22 | 郑州大学 | Heat supplying device for smoke purification and waste heat recovery |
| CN106123313A (en) * | 2016-06-27 | 2016-11-16 | 无锡锡能锅炉有限公司 | A kind of gas fired-boiler heat transmission equipment |
| CN107013896A (en) * | 2017-04-10 | 2017-08-04 | 苏州庆丰包装材料有限公司 | For the steam supply system in production |
| CN107013896B (en) * | 2017-04-10 | 2024-03-12 | 江门市骏腾实业有限公司 | Steam supply system for paperboard production |
| CN107478070A (en) * | 2017-09-24 | 2017-12-15 | 贵州电力设计研究院 | A kind of fountain flue gas water- to-water heat exchanger for generating set |
| CN107990744A (en) * | 2017-12-08 | 2018-05-04 | 佘峰 | A kind of high smelting furnace fume extractor of heat utilization efficiency |
| CN108870427A (en) * | 2018-09-10 | 2018-11-23 | 甘肃红峰机械有限责任公司 | A kind of fume waste heat recyclable device |
| CN109224721A (en) * | 2018-11-21 | 2019-01-18 | 吴迎莉 | A kind of flue gas scrubbing apparatus and method for washing flue gas |
| CN111678354A (en) * | 2020-05-21 | 2020-09-18 | 四川省简阳空冷器制造有限公司 | Method for indirectly cooling air through conversion gas |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150909 Termination date: 20180511 |
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| CF01 | Termination of patent right due to non-payment of annual fee |