CN201059772Y - Boiler heat-recovering and dust cleaning apparatus - Google Patents
Boiler heat-recovering and dust cleaning apparatus Download PDFInfo
- Publication number
- CN201059772Y CN201059772Y CN 200720022943 CN200720022943U CN201059772Y CN 201059772 Y CN201059772 Y CN 201059772Y CN 200720022943 CN200720022943 CN 200720022943 CN 200720022943 U CN200720022943 U CN 200720022943U CN 201059772 Y CN201059772 Y CN 201059772Y
- Authority
- CN
- China
- Prior art keywords
- box
- heat exchanger
- storage tank
- water storage
- fume
- 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.)
- Expired - Fee Related
Links
- 239000000428 dust Substances 0.000 title claims abstract description 10
- 238000004140 cleaning Methods 0.000 title description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 33
- 230000003139 buffering Effects 0.000 claims abstract description 17
- 239000003517 fume Substances 0.000 abstract description 9
- 238000011084 recovery Methods 0.000 abstract description 8
- 239000002918 waste heat Substances 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 26
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,PD94bWwgdmVyc2lvbj0nMS4wJyBlbmNvZGluZz0naXNvLTg4NTktMSc/Pgo8c3ZnIHZlcnNpb249JzEuMScgYmFzZVByb2ZpbGU9J2Z1bGwnCiAgICAgICAgICAgICAgeG1sbnM9J2h0dHA6Ly93d3cudzMub3JnLzIwMDAvc3ZnJwogICAgICAgICAgICAgICAgICAgICAgeG1sbnM6cmRraXQ9J2h0dHA6Ly93d3cucmRraXQub3JnL3htbCcKICAgICAgICAgICAgICAgICAgICAgIHhtbG5zOnhsaW5rPSdodHRwOi8vd3d3LnczLm9yZy8xOTk5L3hsaW5rJwogICAgICAgICAgICAgICAgICB4bWw6c3BhY2U9J3ByZXNlcnZlJwp3aWR0aD0nODVweCcgaGVpZ2h0PSc4NXB4JyB2aWV3Qm94PScwIDAgODUgODUnPgo8IS0tIEVORCBPRiBIRUFERVIgLS0+CjxyZWN0IHN0eWxlPSdvcGFjaXR5OjEuMDtmaWxsOiNGRkZGRkY7c3Ryb2tlOm5vbmUnIHdpZHRoPSc4NS4wJyBoZWlnaHQ9Jzg1LjAnIHg9JzAuMCcgeT0nMC4wJz4gPC9yZWN0Pgo8cGF0aCBjbGFzcz0nYm9uZC0wIGF0b20tMCBhdG9tLTEnIGQ9J00gMjcuNCw0Mi4wIEwgNDMuNSw0Mi4wJyBzdHlsZT0nZmlsbDpub25lO2ZpbGwtcnVsZTpldmVub2RkO3N0cm9rZTojRTg0MjM1O3N0cm9rZS13aWR0aDoxLjBweDtzdHJva2UtbGluZWNhcDpidXR0O3N0cm9rZS1saW5lam9pbjptaXRlcjtzdHJva2Utb3BhY2l0eToxJyAvPgo8cGF0aCBjbGFzcz0nYm9uZC0wIGF0b20tMCBhdG9tLTEnIGQ9J00gNDMuNSw0Mi4wIEwgNTkuNiw0Mi4wJyBzdHlsZT0nZmlsbDpub25lO2ZpbGwtcnVsZTpldmVub2RkO3N0cm9rZTojM0I0MTQzO3N0cm9rZS13aWR0aDoxLjBweDtzdHJva2UtbGluZWNhcDpidXR0O3N0cm9rZS1saW5lam9pbjptaXRlcjtzdHJva2Utb3BhY2l0eToxJyAvPgo8cGF0aCBjbGFzcz0nYm9uZC0wIGF0b20tMCBhdG9tLTEnIGQ9J00gMjcuNCw1My41IEwgNDMuNSw1My41JyBzdHlsZT0nZmlsbDpub25lO2ZpbGwtcnVsZTpldmVub2RkO3N0cm9rZTojRTg0MjM1O3N0cm9rZS13aWR0aDoxLjBweDtzdHJva2UtbGluZWNhcDpidXR0O3N0cm9rZS1saW5lam9pbjptaXRlcjtzdHJva2Utb3BhY2l0eToxJyAvPgo8cGF0aCBjbGFzcz0nYm9uZC0wIGF0b20tMCBhdG9tLTEnIGQ9J00gNDMuNSw1My41IEwgNTkuNiw1My41JyBzdHlsZT0nZmlsbDpub25lO2ZpbGwtcnVsZTpldmVub2RkO3N0cm9rZTojM0I0MTQzO3N0cm9rZS13aWR0aDoxLjBweDtzdHJva2UtbGluZWNhcDpidXR0O3N0cm9rZS1saW5lam9pbjptaXRlcjtzdHJva2Utb3BhY2l0eToxJyAvPgo8cGF0aCBjbGFzcz0nYm9uZC0wIGF0b20tMCBhdG9tLTEnIGQ9J00gMjcuNCwzMC41IEwgNDMuNSwzMC41JyBzdHlsZT0nZmlsbDpub25lO2ZpbGwtcnVsZTpldmVub2RkO3N0cm9rZTojRTg0MjM1O3N0cm9rZS13aWR0aDoxLjBweDtzdHJva2UtbGluZWNhcDpidXR0O3N0cm9rZS1saW5lam9pbjptaXRlcjtzdHJva2Utb3BhY2l0eToxJyAvPgo8cGF0aCBjbGFzcz0nYm9uZC0wIGF0b20tMCBhdG9tLTEnIGQ9J00gNDMuNSwzMC41IEwgNTkuNiwzMC41JyBzdHlsZT0nZmlsbDpub25lO2ZpbGwtcnVsZTpldmVub2RkO3N0cm9rZTojM0I0MTQzO3N0cm9rZS13aWR0aDoxLjBweDtzdHJva2UtbGluZWNhcDpidXR0O3N0cm9rZS1saW5lam9pbjptaXRlcjtzdHJva2Utb3BhY2l0eToxJyAvPgo8dGV4dCB4PSczLjQnIHk9JzUzLjUnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6MjJweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID5PPC90ZXh0Pgo8dGV4dCB4PScxOS4yJyB5PSc0NC4zJyBjbGFzcz0nYXRvbS0wJyBzdHlsZT0nZm9udC1zaXplOjE1cHg7Zm9udC1zdHlsZTpub3JtYWw7Zm9udC13ZWlnaHQ6bm9ybWFsO2ZpbGwtb3BhY2l0eToxO3N0cm9rZTpub25lO2ZvbnQtZmFtaWx5OnNhbnMtc2VyaWY7dGV4dC1hbmNob3I6c3RhcnQ7ZmlsbDojRTg0MjM1JyA+KzwvdGV4dD4KPHRleHQgeD0nNjAuNicgeT0nNTMuNScgY2xhc3M9J2F0b20tMScgc3R5bGU9J2ZvbnQtc2l6ZToyMnB4O2ZvbnQtc3R5bGU6bm9ybWFsO2ZvbnQtd2VpZ2h0Om5vcm1hbDtmaWxsLW9wYWNpdHk6MTtzdHJva2U6bm9uZTtmb250LWZhbWlseTpzYW5zLXNlcmlmO3RleHQtYW5jaG9yOnN0YXJ0O2ZpbGw6IzNCNDE0MycgPkM8L3RleHQ+Cjx0ZXh0IHg9Jzc2LjUnIHk9JzQ0LjMnIGNsYXNzPSdhdG9tLTEnIHN0eWxlPSdmb250LXNpemU6MTVweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiMzQjQxNDMnID4tPC90ZXh0Pgo8L3N2Zz4K [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 6
- 239000003546 flue gas Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 2
- 230000000903 blocking Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
- F28D7/1615—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation the conduits being inside a casing and extending at an angle to the longitudinal axis of the casing; the conduits crossing the conduit for the other heat exchange medium
- F28D7/1623—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation the conduits being inside a casing and extending at an angle to the longitudinal axis of the casing; the conduits crossing the conduit for the other heat exchange medium with particular pattern of flow of the heat exchange media, e.g. change of flow direction
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D21/0001—Recuperative heat exchangers
- F28D21/0003—Recuperative heat exchangers the heat being recuperated from exhaust gases
Abstract
The utility model discloses a boiler afterheat recovery and dust removal device, which comprises a water storage tank and a heat exchanger arranged in the water storage tank, a fume inlet, a fume outlet, a water inlet pipe, a water outlet pipe and an exhaust pipe arranged on the water storage tank, wherein, the fume inlet and the fume outlet are communicated through the heat exchanger, the heat exchanger is composed of an air inlet connecting box, an air outlet connecting box, a heat exchanger and a buffering settlement box, the air inlet connecting box and the air outlet connecting box are arranged at the upper part of the water storage tank, and respectively connected with the fume inlet and the fume outlet, the buffering settlement box is arranged at the lower part of the water storage tank, a dust removal opening is arranged at the bottom part of the water storage tank, and the air inlet connecting box and the air outlet connecting box are communicated through the heat exchanger and the buffering settlement box. Most of fume is displaced into the water in the water storage tank when the high temperature fume passes through, the heat recovery rate is high, the temperature of the heat exchanger is relatively low when being dipped into the water, the service life is long, the heat recovery rate of the utility model is high, the service life is high, and the utility model has both the recovery of waste heat function and the dust removal function.
Description
Technical field
The utility model belongs to boiler afterheat and utilizes technical field, the device that specifically relates to a kind of recovery boiler flue gas heat energy and carry out dedusting.
Background technology
Be effective use of energy sources and minimizing environmental pollution, high-temperature flue gas to the boiler generation, it is people's extensive concern and the problem being devoted to solve in recent years that dirt falls in heat energy recycle and dedusting, the existing method of generally using is between boiler and chimney heat-exchanger rig to be set, existing heat-exchanger rig exists several respects shortcoming: the one, and the thermal efficiency is lower, and heat energy is not utilized effectively in the flue gas; The 2nd, corrosion-resistant, service life is short; The 3rd, function singleness, dust removing effects is poor.
Summary of the invention
The technical problems to be solved in the utility model provides a kind of heat recovery rate height, and long service life has the device of waste heat recovery and dedusting function concurrently.
For solving the problems of the technologies described above, the utility model comprises water storage tank and the heat exchanger that is located at wherein, water storage tank is provided with gas approach, exhanst gas outlet, water inlet pipe, outlet pipe and blast pipe, gas approach and exhanst gas outlet are connected by heat exchanger, its design feature is that heat exchanger is by the air inlet connecting box, the gas outlet connecting box, heat exchanger tube and buffering flow tank are formed, air inlet connecting box and gas outlet connecting box are located at water storage tank top, and join with gas approach and exhanst gas outlet respectively, the buffering flow tank is located at the water storage tank bottom, its bottom is provided with the dedusting mouth, and air inlet connecting box and gas outlet connecting box are connected with the buffering flow tank by heat exchanger tube.
Be provided with two groups of heat exchanger tubes between air inlet connecting box, gas outlet connecting box and buffering flow tank, heat exchanger tube is provided with conducting strip outward.
The beneficial effects of the utility model are: owing to be provided with in water storage tank by the air inlet connecting box, the gas outlet connecting box, the heat exchanger that heat exchanger tube and buffering flow tank are formed, during the heat exchanger tube of high-temperature flue gas by heat exchanger most of heat is discharged in the water of water storage tank, the heat recovery rate height, heat exchanger is under water, temperature is relatively low, not fragile, long service life, the heat exchanger tube inwall is convenient to clean in space in air inlet connecting box and the gas outlet connecting box, prevented that effectively heat exchanger tube from blocking with not smooth, water tank bottom is provided with the buffering flow tank, behind the flue gas cool-down, dust energy rapid subsidence, and can remove from the dedusting mouth of its bottom.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further described:
Fig. 1 is the utility model vertical profile schematic diagram;
Fig. 2 is the A-A cut-away view of this Fig. 1.
Among the figure: 1, water storage tank, 2, heat exchanger, 3, heat exchanger tube, 4, conducting strip, 5, gas approach, 6, exhanst gas outlet, 7, buffering flow tank, 8, the dedusting mouth, 9, water inlet pipe, 10, outlet pipe, 11, blast pipe, 12, overflow pipe, 13, blow-off pipe, 14, air inlet connecting box, 15, the gas outlet connecting box.
The specific embodiment
Boiler afterheat illustrated in figures 1 and 2 reclaims and dust arrester, comprise water storage tank 1 and the heat exchanger 2 that is located at wherein, water storage tank 1 is provided with gas approach 5, exhanst gas outlet 6, water inlet pipe 9, outlet pipe 10 and blast pipe 11, its top and bottom also are respectively equipped with overflow pipe 12 and blow-off pipe 13, gas approach 5 and exhanst gas outlet 6 are connected by heat exchanger 2, heat exchanger 2 is by air inlet connecting box 14, gas outlet connecting box 15, heat exchanger tube 3 and buffering flow tank 7 are formed, air inlet connecting box 14 and gas outlet connecting box 15 are located at water storage tank 1 top, and join with gas approach 5 and exhanst gas outlet 6 respectively, buffering flow tank 7 is located at water storage tank 1 bottom, its bottom is provided with dedusting mouth 8, air inlet connecting box 14, be provided with two groups of heat exchanger tubes 3 between gas outlet connecting box 15 and the buffering flow tank 7, the heat exchanger tube 3 outer conducting strips 4 that are provided with.
During use, gas approach 5 and exhanst gas outlet 6 join with boiler flue gas outlet and chimney respectively, reclaim fume afterheat by heat exchanger.
Claims (2)
1. a boiler afterheat reclaims and dust arrester, comprise water storage tank (1) and be located at wherein heat exchanger (2), water storage tank (1) is provided with gas approach (5), exhanst gas outlet (6), water inlet pipe (9), outlet pipe (10) and blast pipe (11), gas approach (5) and exhanst gas outlet (6) are connected by heat exchanger (2), it is characterized in that: heat exchanger (2) is by air inlet connecting box (14), gas outlet connecting box (15), heat exchanger tube (3) and buffering flow tank (7) are formed, air inlet connecting box (14) and gas outlet connecting box (15) are located at water storage tank (1) top, and join with gas approach (5) and exhanst gas outlet (6) respectively, buffering flow tank (7) is located at water storage tank (1) bottom, its bottom is provided with dedusting mouth (8), and air inlet connecting box (14) and gas outlet connecting box (14) are connected with buffering flow tank (7) by heat exchanger tube (3).
2. reclaim and dust arrester according to the described boiler afterheat of claim 1, it is characterized in that being provided with two groups of heat exchanger tubes (3) between air inlet connecting box (14), gas outlet connecting box (14) and the buffering flow tank (7), the outer conducting strip (4) that is provided with of heat exchanger tube (3).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200720022943 CN201059772Y (en) | 2007-05-30 | 2007-05-30 | Boiler heat-recovering and dust cleaning apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200720022943 CN201059772Y (en) | 2007-05-30 | 2007-05-30 | Boiler heat-recovering and dust cleaning apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
CN201059772Y true CN201059772Y (en) | 2008-05-14 |
Family
ID=39408247
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200720022943 Expired - Fee Related CN201059772Y (en) | 2007-05-30 | 2007-05-30 | Boiler heat-recovering and dust cleaning apparatus |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN201059772Y (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104089501A (en) * | 2014-07-28 | 2014-10-08 | 姚飞燕 | Heat energy exchange device |
CN105972628A (en) * | 2016-05-28 | 2016-09-28 | 许昌东方热力有限公司 | Chimney waste heat recycling system |
CN109099450A (en) * | 2018-08-24 | 2018-12-28 | 章丽霞 | A kind of boiler waste heat recovery system |
-
2007
- 2007-05-30 CN CN 200720022943 patent/CN201059772Y/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104089501A (en) * | 2014-07-28 | 2014-10-08 | 姚飞燕 | Heat energy exchange device |
CN104089501B (en) * | 2014-07-28 | 2015-11-04 | 姚飞燕 | Thermal energy exchange equipment |
CN105972628A (en) * | 2016-05-28 | 2016-09-28 | 许昌东方热力有限公司 | Chimney waste heat recycling system |
CN105972628B (en) * | 2016-05-28 | 2018-07-13 | 许昌东方热力有限公司 | A kind of chimney waste heat recovery system |
CN109099450A (en) * | 2018-08-24 | 2018-12-28 | 章丽霞 | A kind of boiler waste heat recovery system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN205980859U (en) | Surplus heat collecting of boiler recycles device | |
CN201059772Y (en) | Boiler heat-recovering and dust cleaning apparatus | |
CN104832934B (en) | A kind of boiler smoke dedusting waste heat recovering energy conserving device | |
CN101619376B (en) | System for recovering converter gas sensible heat | |
CN201449193U (en) | Boiler flue gas waste heat recovery device | |
CN203479061U (en) | Waste-heat recovery device of high-temperature flue gas | |
CN205897905U (en) | Modular residual heat from flue gas device | |
CN203177191U (en) | Boiler back dedusting and flue gas waste heat recovery integrated device | |
CN205642093U (en) | Waste heat utilization cyclone | |
CN205014401U (en) | Waste heat, coal tar recovery system for boiler | |
CN205482504U (en) | But fluoroplastics tubular heat exchanger structure that level was placed | |
CN203928799U (en) | Dedusting Natural Circulation augmentation of heat transfer flue gas waste heat recovery apparatus | |
CN205412574U (en) | Flue gas waste heat utilization and dust removal and desulfurization device | |
CN201488593U (en) | Device for recovering afterheat of waste gas in boiler | |
CN207294699U (en) | Cold process system between a kind of novel powdered coal temperature gasification and high dedusting | |
CN103471421A (en) | High-temperature flue gas waste heat recovery device and waste heat recovery method of device | |
CN202835452U (en) | Dust removal and heat exchange device suitable for biomass fuel | |
CN203907648U (en) | Spraying drainage type exhaust gas heat exchange device | |
CN2405644Y (en) | Electric stone-ash collecting device | |
CN201106841Y (en) | Boiler economizer | |
CN201697510U (en) | Waste gas afterheat recovery device | |
CN209828585U (en) | Calcium carbide furnace gas purifying and dust removing device | |
CN201497398U (en) | High-efficiency automatic dust-removing heat exchanger | |
CN214620105U (en) | Heat energy recovery biomass boiler for supplying industrial hot water and domestic water with waste heat | |
CN201259206Y (en) | Glass kiln power generation boiler by waste heat |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080514 |