CN111097280A - Anti-sedimentation arrangement process for slurry of internal circulation desulfurization tower - Google Patents
Anti-sedimentation arrangement process for slurry of internal circulation desulfurization tower Download PDFInfo
- Publication number
- CN111097280A CN111097280A CN201911335238.9A CN201911335238A CN111097280A CN 111097280 A CN111097280 A CN 111097280A CN 201911335238 A CN201911335238 A CN 201911335238A CN 111097280 A CN111097280 A CN 111097280A
- Authority
- CN
- China
- Prior art keywords
- slurry
- tower
- area
- internal circulation
- oxidation aeration
- 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.)
- Pending
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/80—Semi-solid phase processes, i.e. by using slurries
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/96—Regeneration, reactivation or recycling of reactants
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/40—Alkaline earth metal or magnesium compounds
- B01D2251/404—Alkaline earth metal or magnesium compounds of calcium
Abstract
The invention discloses an anti-sedimentation arrangement process for slurry of an internal circulation desulfurization tower; the invention effectively solves the problem that the slurry precipitation in the slurry area of the internal circulation desulfurization tower in the lime-gypsum method desulfurization process causes the blockage of the tower bottom and the pipeline, thereby ensuring the long-term continuous and stable operation of the desulfurization system. Compared with the conventional internal circulation desulfurization tower slurry area for preventing slurry sedimentation, the symmetrical stirring device is arranged, and the purpose of preventing slurry sedimentation in the slurry area can be achieved only by adjusting the positions of the inlet of the slurry circulating pump and the oxidation aeration pipe.
Description
Technical Field
The invention relates to the field of desulfurization tower slurry anti-precipitation correlation, in particular to an internal circulation desulfurization tower slurry anti-precipitation arrangement process.
Background
The slurry sedimentation in the slurry area of the internal circulation desulfurization tower in the traditional lime-gypsum method desulfurization process at present easily causes the blockage of the tower bottom and the pipeline, and the long-term continuous and stable operation of a desulfurization system is inevitably influenced; improvements are needed.
Disclosure of Invention
Therefore, in order to solve the above-mentioned disadvantages, the present invention provides an arrangement process for preventing the precipitation of slurry in an internal circulation desulfurization tower; the invention effectively solves the problem that the slurry precipitation in the slurry area of the internal circulation desulfurization tower in the lime-gypsum method desulfurization process causes the blockage of the tower bottom and the pipeline, thereby ensuring the long-term continuous and stable operation of the desulfurization system. Compared with the conventional internal circulation desulfurization tower slurry area for preventing slurry sedimentation, the symmetrical stirring device is arranged, and the purpose of preventing slurry sedimentation in the slurry area can be achieved only by adjusting the positions of the inlet of the slurry circulating pump and the oxidation aeration pipe.
The invention is realized in such a way, and the anti-sedimentation arrangement process for the slurry of the internal circulation desulfurization tower is constructed, and is characterized in that: the method is realized as follows; enabling the inlet of the slurry circulating pump to be in 360-degree equal distribution and then to be in tangential arrangement in the slurry area of the tower kettle, and enabling the slurry in the inner layer and the outer layer of the slurry area of the tower kettle to rotate along the tower wall by utilizing the suction force of the inlet of the slurry circulating pump to be in tangential distribution;
three sets of oxidation aeration pipes are uniformly distributed at 120 degrees in the slurry area of the tower kettle, and one oxidation aeration pipe is distributed at the center of the slurry area of the tower kettle;
the inner layer slurry in the slurry area of the tower kettle is rotated by utilizing tangential thrust generated during aeration of the oxidation aeration pipe, and the oxidation aeration pipe is arranged at the center of the slurry area, so that the accumulation of particles in the slurry at the center of the tower bottom due to the rotation of the slurry in the tower is avoided; therefore, the invention effectively avoids the blockage of the tower bottom and the pipeline caused by the slurry sedimentation in the slurry area of the internal circulation desulfurization tower by adjusting the positions of the inlet of the slurry circulating pump and the oxidation aeration pipe.
The invention relates to an anti-precipitation arrangement process for slurry of an internal circulation desulfurization tower, which is characterized in that: three sets of oxidation aeration pipes are uniformly distributed at 120 degrees in the tower bottom slurry area, wherein the height of a pipe orifice from the tower bottom plate is 650mm, the outlet direction is distributed downwards at 120 degrees along the circumferential tangential direction, one oxidation aeration pipe is distributed at the center of the tower bottom slurry area, the height of the pipe orifice from the tower bottom plate is 650mm, and the outlet direction is vertical downwards.
The invention has the following advantages: the invention provides an anti-precipitation arrangement process for slurry of an internal circulation desulfurization tower; the invention effectively solves the problem that the slurry precipitation in the slurry area of the internal circulation desulfurization tower in the lime-gypsum method desulfurization process causes the blockage of the tower bottom and the pipeline, thereby ensuring the long-term continuous and stable operation of the desulfurization system. Compared with the conventional internal circulation desulfurization tower slurry area for preventing slurry sedimentation, the symmetrical stirring device is arranged, and the purpose of preventing slurry sedimentation in the slurry area can be achieved only by adjusting the positions of the inlet of the slurry circulating pump and the oxidation aeration pipe.
Drawings
FIG. 1 is a diagram of a circulation pump inlet arrangement;
fig. 2-3 are arrangement diagrams of oxidation aeration pipes.
Detailed Description
The present invention will be described in detail with reference to fig. 1 to 3, and the technical solutions in the embodiments of the present invention will be clearly and completely described, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
The invention provides an internal circulation desulfurization tower slurry anti-sedimentation arrangement process through improvement, the inlet of a slurry circulating pump is arranged tangentially after being equally divided by 360 degrees in a tower kettle slurry area, and the slurry in the inner layer and the outer layer of the tower kettle slurry area rotates along the tower wall by utilizing the suction force of the inlet of the slurry circulating pump in tangential distribution. Three sets of oxidation aeration pipes are uniformly distributed at 120 degrees in the slurry area of the tower kettle (the pipe orifice is 650mm away from the bottom plate of the tower, the outlet direction is downwards distributed at 120 degrees along the circumferential tangential direction), and one oxidation aeration pipe is distributed at the center of the slurry area of the tower kettle (the pipe orifice is 650mm away from the bottom plate of the tower, and the outlet direction is vertically downwards). The inner layer slurry in the slurry area of the tower kettle is rotated by utilizing tangential thrust generated during aeration of the oxidation aeration pipe, and the oxidation aeration pipe is arranged at the center of the slurry area, so that the phenomenon that particles in the slurry are accumulated at the center of the tower bottom due to rotation of the slurry in the tower is avoided. Therefore, the invention effectively avoids the blockage of the tower bottom and the pipeline caused by the slurry sedimentation in the slurry area of the internal circulation desulfurization tower by adjusting the positions of the inlet of the slurry circulating pump and the oxidation aeration pipe. The invention cancels three stirrers in the slurry area of the internal circulation tower, reduces the primary investment cost and the operation and maintenance cost, and achieves the purposes of environmental protection, energy conservation and emission reduction.
The previous description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the generic principles defined herein may be applied to other embodiments without departing from the spirit or scope of the invention. Thus, the present invention is not intended to be limited to the embodiments shown herein but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
Claims (2)
1. An internal circulation desulfurization tower slurry anti-precipitation arrangement process is characterized in that: the method is realized as follows; enabling the inlet of the slurry circulating pump to be in 360-degree equal distribution and then to be in tangential arrangement in the slurry area of the tower kettle, and enabling the slurry in the inner layer and the outer layer of the slurry area of the tower kettle to rotate along the tower wall by utilizing the suction force of the inlet of the slurry circulating pump to be in tangential distribution;
three sets of oxidation aeration pipes are uniformly distributed at 120 degrees in the slurry area of the tower kettle, and one oxidation aeration pipe is distributed at the center of the slurry area of the tower kettle;
the inner layer slurry in the slurry area of the tower kettle is rotated by utilizing tangential thrust generated during aeration of the oxidation aeration pipe, and the oxidation aeration pipe is arranged at the center of the slurry area, so that the accumulation of particles in the slurry at the center of the tower bottom due to the rotation of the slurry in the tower is avoided; therefore, the invention effectively avoids the blockage of the tower bottom and the pipeline caused by the slurry sedimentation in the slurry area of the internal circulation desulfurization tower by adjusting the positions of the inlet of the slurry circulating pump and the oxidation aeration pipe.
2. The internal circulation desulfurization tower slurry anti-settling arrangement process as claimed in claim 1, wherein: three sets of oxidation aeration pipes are uniformly distributed at 120 degrees in the tower bottom slurry area, wherein the height of a pipe orifice from the tower bottom plate is 650mm, the outlet direction is distributed downwards at 120 degrees along the circumferential tangential direction, one oxidation aeration pipe is distributed at the center of the tower bottom slurry area, the height of the pipe orifice from the tower bottom plate is 650mm, and the outlet direction is vertical downwards.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911335238.9A CN111097280A (en) | 2019-12-23 | 2019-12-23 | Anti-sedimentation arrangement process for slurry of internal circulation desulfurization tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201911335238.9A CN111097280A (en) | 2019-12-23 | 2019-12-23 | Anti-sedimentation arrangement process for slurry of internal circulation desulfurization tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN111097280A true CN111097280A (en) | 2020-05-05 |
Family
ID=70423789
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201911335238.9A Pending CN111097280A (en) | 2019-12-23 | 2019-12-23 | Anti-sedimentation arrangement process for slurry of internal circulation desulfurization tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN111097280A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203790824U (en) * | 2014-02-19 | 2014-08-27 | 石福军 | High-efficiency boiler smoke desulphurization tower |
| US20170198908A1 (en) * | 2014-09-29 | 2017-07-13 | Beijing Spc Environment Protection Tech Co., Ltd. | Rotational flow and sink flow-coupling integrated system for ultra-clean desulphuration and dedusting and desulphuration and dedusting method therefor |
| CN107185385A (en) * | 2017-07-07 | 2017-09-22 | 金川集团股份有限公司 | A kind of spuious flue gas during smelting wet dedusting of atm number, sulfur method |
| CN207430031U (en) * | 2017-08-09 | 2018-06-01 | 南京中电环保科技有限公司 | Absorption tower pulse-type disturbance device and absorption tower |
| CN109173688A (en) * | 2018-11-05 | 2019-01-11 | 山东国舜建设集团有限公司 | One kind is from stirring-type absorption tower |
| KR102042974B1 (en) * | 2019-08-26 | 2019-11-11 | 두산중공업 주식회사 | Wet desulfurization apparatus with divided slurry storage improving desulfurization efficiency and wet desulfurization method using the same |
-
2019
- 2019-12-23 CN CN201911335238.9A patent/CN111097280A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203790824U (en) * | 2014-02-19 | 2014-08-27 | 石福军 | High-efficiency boiler smoke desulphurization tower |
| US20170198908A1 (en) * | 2014-09-29 | 2017-07-13 | Beijing Spc Environment Protection Tech Co., Ltd. | Rotational flow and sink flow-coupling integrated system for ultra-clean desulphuration and dedusting and desulphuration and dedusting method therefor |
| CN107185385A (en) * | 2017-07-07 | 2017-09-22 | 金川集团股份有限公司 | A kind of spuious flue gas during smelting wet dedusting of atm number, sulfur method |
| CN207430031U (en) * | 2017-08-09 | 2018-06-01 | 南京中电环保科技有限公司 | Absorption tower pulse-type disturbance device and absorption tower |
| CN109173688A (en) * | 2018-11-05 | 2019-01-11 | 山东国舜建设集团有限公司 | One kind is from stirring-type absorption tower |
| KR102042974B1 (en) * | 2019-08-26 | 2019-11-11 | 두산중공업 주식회사 | Wet desulfurization apparatus with divided slurry storage improving desulfurization efficiency and wet desulfurization method using the same |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105920962B (en) | A kind of chimney leftover bits and pieces water bath dust-removing sulfur method | |
| CN210964759U (en) | Slurry mixing device | |
| CN102080671B (en) | Centrifugal pump | |
| CN111097280A (en) | Anti-sedimentation arrangement process for slurry of internal circulation desulfurization tower | |
| EP3258063A1 (en) | Axial flow turbine | |
| CN211575545U (en) | High-efficiency flow-guiding heat-insulating water tank and flow guider thereof | |
| CN210127117U (en) | Advanced oxidation reactor | |
| CN206289044U (en) | Laboratory anaerobic reactor hydraulic pressure rotation water-locator | |
| CN210176492U (en) | Water distribution structure | |
| CN205127949U (en) | Reation kettle with condensing agent recovery unit | |
| CN206391859U (en) | Centrifugal flue gas device for deep cleaning and desulfurizing tower with flow splitter | |
| CN208482460U (en) | A kind of stainless steel reaction tank reinforcing rabbling mechanism | |
| CN202718451U (en) | Corrosion-resistant and energy-saving dust-collecting chimney | |
| CN202654922U (en) | Smoke desulfurizing tower for preventing bottom suspended solids from depositing | |
| CN106422740A (en) | Centrifugal type deep flue gas purification device provided with shunting ring and desulfurization tower | |
| CN111675317A (en) | Hydrolysis acidification pool for suspended filler | |
| CN208606157U (en) | A kind of Direct Air-Cooled photo-thermal unit and its water replanishing device | |
| CN207203553U (en) | A kind of vertically placed type sedimentation basin | |
| CN206081993U (en) | Derotation formula swirl purifying column | |
| CN217350905U (en) | Rotational flow water distributor | |
| CN212076776U (en) | Sludge discharge device based on air stripping principle | |
| CN210814624U (en) | Flue of flue gas desulfurization reactor | |
| CN214115061U (en) | Anaerobic water distribution device | |
| CN204625222U (en) | Telescopic mixing reactor | |
| CN216046092U (en) | Anti-blocking water distributor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20200505 |
|
| RJ01 | Rejection of invention patent application after publication |