CN102949928A - Viscous flue gas removal device - Google Patents
Viscous flue gas removal device Download PDFInfo
- Publication number
- CN102949928A CN102949928A CN 201210416579 CN201210416579A CN102949928A CN 102949928 A CN102949928 A CN 102949928A CN 201210416579 CN201210416579 CN 201210416579 CN 201210416579 A CN201210416579 A CN 201210416579A CN 102949928 A CN102949928 A CN 102949928A
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- adsorbent
- flue gas
- ash
- jet pump
- viscous
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Abstract
The invention discloses a viscous flue gas removal device, comprising an injection pump, a compressed air blowing pipe, an adsorbent nozzle, a connecting pipe, an ash removal spiral and a novel adsorbent storage cabin. The injection pump is installed outside the bag type dust collector, and is provided with the compressed air blowing pipe; the adsorbent nozzle is arranged in an air inlet of the dust collector, and is connected to the injection pump through a connecting pipe; the ash removal end of the ash removal spiral is connected with an ash bucket of the dust collector, and an ash sending end is connected with the injection pump; and the novel adsorbent storage cabin is arranged on the ash removal spiral, and can spray adsorbent into the ash removal spiral. The viscous flue gas removal device can improve usage efficiency of the adsorbent, and reduce operating cost on viscous flue gas removal.
Description
Technical field
The present invention relates to a kind of except the viscosity flue gas device.
Background technology
A large amount of mist of oil, dust and the tar of content in the flue gas of oil burning boiler industrial equipment discharging, dust collected in the flue gas has adhesiveness.These adhesiveness flue gases and dust can make the filter bag " stick with paste bag " of sack cleaner in the dust removal process of sack cleaner, namely form viscosity muffin layer on the filter bag surface, and easy-clear not affects the normal ventilation of sack cleaner even can not normally use.
Existing dust collecting process is to enter at the viscosity flue gas to spray into adsorbent in the sack cleaner forward direction viscosity flue gas and remove dust viscosity, but in this kind technique owing to adsorbent and viscosity flue gas incorporation time is short, reaction not exclusively cause the adsorbent service efficiency low, except the operating cost of viscosity flue gas high.
Summary of the invention
The technical problem to be solved in the present invention provides a kind of except the viscosity flue gas device, can improve the service efficiency of adsorbent, reduces the operating cost except the viscosity flue gas.
For solving the problems of the technologies described above, the present invention is a kind of except the viscosity flue gas device, be blown into pipe, adsorbent nozzle, connecting pipe, get grey spiral and the novel sorbents bunker forms by jet pump, compressed air, jet pump is installed in the sack cleaner outside, jet pump is provided with compressed air and is blown into pipe, the adsorbent nozzle is arranged in the deduster air inlet, the adsorbent nozzle links to each other with jet pump by connecting pipe, the ash end of getting of getting grey spiral is connected with dust collector ash hopper, send the ash end to be connected with jet pump, the novel sorbents bunker is arranged on to be got on the grey spiral, can spray into adsorbent to it.
In the dust removal process, fall into dust collector ash hopper with dust after adsorbent and the reaction of viscosity flue gas partial, getting the part dust of the adsorbent that contains incomplete use that grey spiral will collect extracts out, send into jet pump, compressed air is blown into the compressed air that pipe is blown into dust is sprayed at a high speed, spray from the adsorbent nozzle through after the connecting pipe, again enter sack cleaner from the deduster air inlet, viscosity composition in the absorption flue gas, be repeatedly used like this, improve the service efficiency of adsorbent, reduced the operating cost except the viscosity flue gas.
In use for some time, mainly be that the Dust Capacity in the dust collector ash hopper accumulates to when needing to discharge, dust is discharged, when discharging dust, enter from the additional part novel sorbents of novel sorbents bunker again and get grey spiral, satisfy the needs of removing the viscosity composition.
Description of drawings
To be that the present invention is a kind of be installed in structural representation on the sack cleaner except the viscosity flue gas device to Fig. 1.
1. get grey spiral among the figure, 2. novel sorbents bunker, and 3. compressed air is blown into pipe, 4. jet pump, 5. connecting pipe, 6. deduster air inlet, 7. adsorbent nozzle, 8. dust collector ash hopper.
The specific embodiment
Among Fig. 1, a kind of except the viscosity flue gas device, be blown into pipe 3, adsorbent nozzle 7, connecting pipe 5, get grey spiral 1 and novel sorbents bunker 2 forms by jet pump 4, compressed air, jet pump 4 is installed in the sack cleaner outside, jet pump 4 is provided with compressed air and is blown into pipe 3, adsorbent nozzle 7 is arranged in the deduster air inlet 6, adsorbent nozzle 7 links to each other with jet pump 4 by connecting pipe 5, the ash end of getting of getting grey spiral 1 is connected with dust collector ash hopper 8, send the ash end to be connected with jet pump 4, novel sorbents bunker 2 is arranged on to be got on the grey spiral 1, can spray into adsorbent to it.
In the dust removal process, fall into dust collector ash hopper 8 with dust after adsorbent and the reaction of viscosity flue gas partial, getting the part dust of the adsorbent that contains incomplete use that grey spiral 1 will collect extracts out, send into jet pump 4, compressed air is blown into pipe 3 compressed air that are blown into dust is sprayed at a high speed, through spraying from adsorbent nozzle 7 after the connecting pipe 5, again enter sack cleaner from deduster air inlet 6, viscosity composition in the absorption flue gas, be repeatedly used like this, improve the service efficiency of adsorbent, reduced the operating cost except the viscosity flue gas.
In use for some time, mainly be that the Dust Capacity in the dust collector ash hopper 8 accumulates to when needing to discharge, dust is discharged, when discharging dust, enter from novel sorbents bunker 2 additional part novel sorbents again and get grey spiral 1, satisfy the needs of removing the viscosity composition.
Claims (1)
1. one kind is removed the viscosity flue gas device, it is characterized in that: be blown into pipe, adsorbent nozzle, connecting pipe, get grey spiral and the novel sorbents bunker forms by jet pump, compressed air, jet pump is installed in the sack cleaner outside, jet pump is provided with compressed air and is blown into pipe, the adsorbent nozzle is arranged in the deduster air inlet, the adsorbent nozzle links to each other with jet pump by connecting pipe, the ash end of getting of getting grey spiral is connected with dust collector ash hopper, send the ash end to be connected with jet pump, the novel sorbents bunker is arranged on to be got on the grey spiral, can spray into adsorbent to it.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201210416579 CN102949928A (en) | 2012-10-27 | 2012-10-27 | Viscous flue gas removal device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201210416579 CN102949928A (en) | 2012-10-27 | 2012-10-27 | Viscous flue gas removal device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102949928A true CN102949928A (en) | 2013-03-06 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201210416579 Pending CN102949928A (en) | 2012-10-27 | 2012-10-27 | Viscous flue gas removal device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102949928A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103727013A (en) * | 2013-12-27 | 2014-04-16 | 宁夏共享集团有限责任公司 | Multi-stage vacuum pump |
| CN104958960A (en) * | 2015-05-26 | 2015-10-07 | 杭州南方环境净化设备有限公司 | Quantitative environmentally-friendly powder sprayer and powder spray dedusting method |
| CN108554048A (en) * | 2018-01-08 | 2018-09-21 | 河北蓝纯环境科技有限公司 | The dry process technique and dry process equipment of exhaust gas containing sticky dust |
| CN108671698A (en) * | 2018-05-13 | 2018-10-19 | 湖南钜晟环保科技工程有限公司 | A kind of exhaust gas adsorption box |
-
2012
- 2012-10-27 CN CN 201210416579 patent/CN102949928A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103727013A (en) * | 2013-12-27 | 2014-04-16 | 宁夏共享集团有限责任公司 | Multi-stage vacuum pump |
| CN104958960A (en) * | 2015-05-26 | 2015-10-07 | 杭州南方环境净化设备有限公司 | Quantitative environmentally-friendly powder sprayer and powder spray dedusting method |
| CN108554048A (en) * | 2018-01-08 | 2018-09-21 | 河北蓝纯环境科技有限公司 | The dry process technique and dry process equipment of exhaust gas containing sticky dust |
| CN108554048B (en) * | 2018-01-08 | 2020-12-04 | 河北蓝纯环境科技有限公司 | Dry treatment process and dry treatment equipment for waste gas containing sticky dust |
| CN108671698A (en) * | 2018-05-13 | 2018-10-19 | 湖南钜晟环保科技工程有限公司 | A kind of exhaust gas adsorption box |
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Legal Events
| Date | Code | Title | Description |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20130306 |