CN109078445A - Flue gas ash removal takes off white integrated apparatus - Google Patents
Flue gas ash removal takes off white integrated apparatus Download PDFInfo
- Publication number
- CN109078445A CN109078445A CN201811225684.XA CN201811225684A CN109078445A CN 109078445 A CN109078445 A CN 109078445A CN 201811225684 A CN201811225684 A CN 201811225684A CN 109078445 A CN109078445 A CN 109078445A
- Authority
- CN
- China
- Prior art keywords
- flue gas
- shell
- ash removal
- integrated apparatus
- takes
- 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
- 239000003546 flue gas Substances 0.000 title claims abstract description 93
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 90
- 239000007789 gas Substances 0.000 claims abstract description 28
- 230000003068 static effect Effects 0.000 claims abstract description 24
- 239000000428 dust Substances 0.000 claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- 238000001816 cooling Methods 0.000 claims abstract description 16
- 238000010438 heat treatment Methods 0.000 claims abstract description 9
- 238000000926 separation method Methods 0.000 claims abstract description 5
- 238000002955 isolation Methods 0.000 claims description 11
- 239000010865 sewage Substances 0.000 claims description 10
- 239000007921 spray Substances 0.000 claims description 9
- 229920006395 saturated elastomer Polymers 0.000 claims description 5
- 238000011010 flushing procedure Methods 0.000 claims description 4
- 239000000498 cooling water Substances 0.000 claims description 3
- 239000007770 graphite material Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 238000005507 spraying Methods 0.000 claims description 2
- 241000270295 Serpentes Species 0.000 claims 1
- 238000009833 condensation Methods 0.000 abstract description 4
- 230000005494 condensation Effects 0.000 abstract description 4
- 239000000779 smoke Substances 0.000 abstract description 4
- 239000000443 aerosol Substances 0.000 abstract description 3
- 238000006477 desulfuration reaction Methods 0.000 abstract description 3
- 230000023556 desulfurization Effects 0.000 abstract description 3
- 239000012716 precipitator Substances 0.000 abstract description 2
- 239000002956 ash Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 6
- 230000007613 environmental effect Effects 0.000 description 5
- 235000019504 cigarettes Nutrition 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000009825 accumulation Methods 0.000 description 2
- 230000005684 electric field Effects 0.000 description 2
- 230000010354 integration Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000004781 supercooling Methods 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000010883 coal ash Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0057—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
-
- 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
- B01D53/002—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 by condensation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Electrostatic Separation (AREA)
- Separating Particles In Gases By Inertia (AREA)
Abstract
The invention discloses a kind of flue gas ash removal, take off white integrated apparatus, it is characterized by comprising shells, the bottom of shell has gas inlet, the cooling condensing unit of wet static dedusting device, water separator, flue gas, demister and Smoke-heating device are arranged in the shell on gas inlet top from bottom to top, flue gas after desulfurization initially enters wet electrical dust precipitator, dust, partial moisture, SO in removing flue gas3After equal aerosols, into the efficient deep condensation dehumidifier of flue gas and Upper separator, further remove the moisture and dust in flue gas, the moisture in flue gas is set to reach≤8.5%, enter top high efficiency heater after the pure flue gas separation moisture of low temperature to heat flue gas temperature raising, flue-gas temperature is improved to 80 DEG C or more, passes through smoke stack emission, ensure that discharge exhaust gas dust content it is low, without white plume, dust content 1.5-2.5mg/Nm3 in flue gas.
Description
Technical field
The present invention relates to a kind of dust-extraction units, specifically, being related to a kind of flue gas ash removal, taking off white integrated apparatus, belong to
Field of mechanical technique.
Background technique
It with the enhancing of people's environmental consciousness, discharges in flue gas dust content and white requirement is taken off to flue gas and be increasingly stringenter, be
The living environment of enhancement of environment people is protected, people are higher and higher to environmental protection requirement, while having to emission request index
Tightened up requirement.
Currently, there are a variety of flue gas ash removals in the market, taking off white technique, but there is a problem of that efficiency of dust collection is low, and
Dust fine in industrial waste gas, coal ash can not often be removed, when discharge pollutes, and if things go on like this easily causes mist
Haze, in the today for increasingly focusing on environmental protection, existing equipment and technique have not adapted to the newest cigarette of current Environmental Protection in China
The requirement of dirt pollutant discharge index, at the same cannot achieve flue gas take off it is white, not only investment it is high but also operation energy consumption is also big.
Summary of the invention
Technical problem to be solved by the invention is to provide a kind of flue gas ash removal, white integrated apparatus is taken off, the device is automatic
Change degree is high, and operating cost is low, and equipment investment is low, and safe and reliable to operation, no pollution to the environment, flue gas reaches minimum discharge, cigarette
Dust (1.5-2.5) mg/Nm3 in gas.
In order to solve the above technical problems, the technical scheme is that flue gas ash removal, taking off white integrated apparatus, feature
Be: including shell, the bottom of shell has gas inlet, and it is quiet to be arranged with wet type from bottom to top in the shell on gas inlet top
The cooling condensing unit of electrical dust collector device, water separator, flue gas, demister and Smoke-heating device.
Further, wet static dedusting device includes several anode tubes, and anode tube includes that section is regular hexagon
Anode and cathode disposed within, the inner wall of anode have graphite material, the distance between anode and cathode 180mm, electricity
Pressure is 80kv, and anode, cathode are connect with the electrode being arranged in outside shell.
Further, water separator includes being arranged on the intracorporal isolation board of shell, isolation board to have several ventilations
Hole and the snorkel being connected to vent seal, the top of snorkel are equipped with tapered cap, the gas outlet of snorkel and tapered cap it
Between there is gap, shell is equipped with discharge outlet, and the height of discharge outlet is consistent with the height of isolation board (12).
Further, the cooling condensing unit of flue gas includes the coil pipe that water separator top is arranged in, and is connected in coil pipe
Recirculated cooling water.
Further, demister includes the blade of several superpositions, and the section of blade is sinusoidal pattern, by PP material system
At being fixed in shell by fixture.
Further, Smoke-heating device is coil heat exchanger, and inside is connected with the saturated vapor of 0.3MPa, coil heat exchanger
It is fixed in shell by fixture.
Further, between gas inlet and wet static dedusting device be equipped with uniform board, enable flue gas equably into
Enter wet static dedusting device.
Further, several spray nozzles, spray spray are equipped between wet static dedusting device and water separator
The water spraying direction of head is downward, when wet static dedusting device power failure is not reruned, regular spraying-rinsing anode tube, and the bottom of shell
Portion has sewage draining exit, and sewage draining exit and gas inlet and exhaust gases passes are mutually isolated.
Further, it is equipped with flusher between the cooling condensing unit of flue gas and demister, if the flusher includes
The dry Flushing nozzle being upwardly or downwardly arranged.
Present invention employs above-mentioned technical proposals, compared with prior art, have the advantage that flue, wet-esp
Device, flue gas condenser, heater and chimney are the integrated design, and solve the problems, such as the dust of flue gas emission and flue gas plume.It is de-
Flue gas initially enters wet electrical dust precipitator, dust, partial moisture, SO in removing flue gas after sulphur3After equal aerosols, into flue gas
Efficient deep condensation dehumidifier and Upper separator further remove moisture and dust in flue gas, reach the moisture in flue gas
To≤8.5%, the harmful substances such as the moisture carried secretly in flue gas are reduced, reduce flue gas environmental pollution.The pure flue gas separation of low temperature
Enter top high efficiency heater after moisture to heat flue gas temperature raising, flue-gas temperature is improved to 80 DEG C or more, by smoke stack emission, is protected
Demonstrate,proved discharge exhaust gas dust content it is low, without white plume, dust content 1.5-2.5mg/Nm3 in flue gas reaches the ultralow row of environmental protection
Standard requirements are put, positive impetus is played to enhancement of environment.
It realizes flue gas ash removal, take off white integration, flue gas reaches minimum discharge, and the plant automation degree is high, operation
At low cost, equipment investment is low, safe and reliable to operation, and no pollution to the environment is easy to operate, and whole system uses modularized design,
It is easily installed and repairs, there is very high popularizing value.
The following describes the present invention in detail with reference to examples.
Detailed description of the invention
Attached drawing 1 is flue gas ash removal in the embodiment of the present invention, the structural schematic diagram for taking off white integrated apparatus；
In figure:
1- shell, 2- gas inlet, 3- wet static dedusting device, 4- water separator, the cooling condensing unit of 5- flue gas, 6-
Demister, 7- Smoke-heating device, 8- anode tube, 9- spray nozzle, 10- sewage draining exit, 11- Flushing nozzle, 12- isolation board,
13- tapered cap, 14- discharge outlet, 15- snorkel, 16- chimney.
Specific embodiment
Embodiment, as shown in Figure 1, flue gas ash removal, taking off white integrated apparatus, including shell 1, the bottom of shell 1 has cigarette
Gas import 2, be arranged in the shell 1 on 2 top of gas inlet from bottom to top wet static dedusting device 3, water separator 4,
Flue gas cools down condensing unit 5, demister 6 and Smoke-heating device 7.
Wet static dedusting device 3 include several anode tubes 8, anode tube 8 include section be regular hexagon anode and
Cathode disposed within, the inner wall of anode have graphite material, and the distance between anode and cathode 180mm, voltage are
80kv, anode, cathode are connect with the electrode being arranged in outside shell 1.
Water separator 4 includes the isolation board that is arranged in shell 1, have on isolation board several ventholes and with it is logical
The snorkel 15 of port sealing connection, the top of snorkel 15 are equipped with tapered cap 13, the gas outlet of snorkel 15 and tapered cap 13
Between there is gap, shell 1 is equipped with discharge outlet 14, and the height of discharge outlet 14 is consistent with the height of isolation board 12.Separate section
Moisture in flue gas, tapered cap 13 and snorkel 15 guarantee the moisture that the cooling condensing unit 5 of flue gas, demister 6 separate
It not can enter in wet static dedusting device 3, guarantee that wet static dedusting device 3 operates normally.
The cooling condensing unit 5 of flue gas includes the coil pipe that 4 top of water separator is arranged in, and is connected with circulating cooling in coil pipe
Water.After flue gas and recirculated cooling water carry out heat exchange, flue gas is made to be cooled to 35 DEG C of the wet cigarette of saturation by 50 DEG C of saturation wet flue gas
Flue gas moisture is precipitated in gas, and moisture is accumulated into drop by steam, isolates partial drop, and further goes to smoke abatement and part
Harmful substance and vapour colloidal sol, flue gas are further purified.
Demister 6 includes the blade of several superpositions, and the section of blade is sinusoidal pattern, is made of PP material, passes through folder
Tool is fixed in shell 1.The drop that will be carried secretly in the flue gas condensed through supercooling, in the flue gas separated through demister 6
Droplet content is down to 20mg/Nm3Below.
Smoke-heating device 7 is coil heat exchanger, and inside is connected with the saturated vapor of 0.3MPa, and coil heat exchanger passes through fixture
It is fixed in shell 1.The clean flue gas by dedusting, condensation, separation demisting is added by coil heat exchanger using steam
Heat, flue gas become 80 DEG C of unsaturated flue gases from 35 DEG C of saturation wet flue gas, so that flue gas is become undersaturated condition from saturation state, pass through
The flue gas of smoke stack emission achievees the purpose that disappear white.
It is equipped with uniform board between gas inlet 2 and wet static dedusting device 3, keeps flue gas quiet evenly into wet type
Electrical dust collector device 3.
Several spray nozzles 9, the spray of spray nozzle 9 are equipped between wet static dedusting device 3 and water separator 4
Water direction is downward, and when the power failure of wet static dedusting device 3 is not reruned, regular spraying-rinsing anode tube 8 opens the valve of bottom
Door, the sewage after cleaning are discharged from the sewage draining exit 10 of bottom, and sewage draining exit 10 and gas inlet 2 and exhaust gases passes are mutually isolated.
Flusher is equipped between the cooling condensing unit 5 of flue gas and demister 6, which includes that several are upward
And down-set Flushing nozzle 11, for cleaning the disk of the bottom of blade and the cooling condensing unit 5 of flue gas in demister 6
Pipe, the sewage after cleaning are fallen on the isolation board 12 of water separator 4, since the top of snorkel is equipped with tapered cap 13, institute
It will not be entered in wet static dedusting device 3 with sewage, influence the operation of wet static dedusting device 3, the discharge outlet from shell 1
14 discharges.
Process flow is as follows:
50 DEG C or so of the saturation wet flue gas after desulfurization, from gas inlet 2 even into wet static dedusting after uniform board
Device 3, the process that ash-laden gas is ionized in the 80kv high voltage electric field by anode tube 8 in wet static dedusting device 3
In, keep grit charged, and grit is moved to anode accumulation under the active force of electric field force, after wet static dedusting device 3,
It separates grit from dusty gas, flue gas is dusted, removes part harmful substance in partial moisture and flue gas
Aerosol, dust content is less than 3mg/Nm in flue gas3。
Flue gas after 3 dedusting of wet static dedusting device enters the cooling condensing unit of flue gas through water separator 4
5 heat exchange, wet flue gas by 50 DEG C or so be down to 35 DEG C hereinafter, moisture in flue gas through supercooling condense (accumulation) most of moisture by
Steam is as droplet, flue gas after cooling (separation moisture goes desulphurization system to re-use) after demister 6 separates moisture,
Flue gas rises to Smoke-heating device 7 and 0.3MPa saturated vapor exchanges heat, and flue gas lifts temperature to 80 DEG C above by chimney by 35 DEG C
16 discharges are saturated wet flue gas by after dedusting, taking off white integration apparatus processing, flue gas is passed through by 50 DEG C of saturated flue gas after desulfurization
It crosses cooling condensation and heats up again and reach undersaturated condition discharge, eliminate discharge flue gas plume.
Measure through test of many times: dust 1.5-2.5mg/Nm3 in the flue gas of discharge meets minimum discharge requirement, disappears simultaneously
In addition to (not having) white plume.
The above is the citing of best mode for carrying out the invention, wherein the part that do not address in detail is that this field is common
The common knowledge of technical staff.Protection scope of the present invention is based on the contents of the claims, any based on technology of the invention
The equivalent transformation of enlightenment and progress, also within protection scope of the present invention.
Claims (9)
1. flue gas ash removal takes off white integrated apparatus, it is characterised in that: including shell (1), the bottom of shell (1) have flue gas into
Mouth (2), the shell (1) on gas inlet (2) top is interior to be arranged with wet static dedusting device (3), steam-water separation dress from bottom to top
Set (4), flue gas cooling condensing unit (5), demister (6) and Smoke-heating device (7).
2. flue gas ash removal as described in claim 1 takes off white integrated apparatus, it is characterised in that: wet static dedusting device (3)
Including several anode tubes (8), anode tube (8) includes the anode and cathode disposed within that section is regular hexagon, anode
Inner wall has graphite material, and the distance between anode and cathode 180mm, voltage 80kv, anode, cathode and setting are in shell
The electrode connection of body (1) outside.
3. flue gas ash removal as described in claim 1 takes off white integrated apparatus, it is characterised in that: water separator (4) includes
Isolation board in shell (1), the snorkel for having several ventholes on isolation board and being connected to vent seal are set
(15), the top of snorkel (15) is equipped with tapered cap (13), between having between the gas outlet and tapered cap (13) of snorkel (15)
Gap, shell (1) are equipped with discharge outlet (14), and the height of discharge outlet (14) is consistent with the height of isolation board (12).
4. flue gas ash removal as described in claim 1 takes off white integrated apparatus, it is characterised in that: flue gas is cooling condensing unit (5)
Including the coil pipe on water separator (4) top is arranged, recirculated cooling water is connected in coil pipe.
5. flue gas ash removal as described in claim 1 takes off white integrated apparatus, it is characterised in that: demister (6) includes several
The section of the blade of a superposition, blade is sinusoidal pattern, is made of PP material, is fixed in shell (1) by fixture.
6. flue gas ash removal as described in claim 1 takes off white integrated apparatus, it is characterised in that: Smoke-heating device (7) is snake
Heat exchange of heat pipe, inside are connected with the saturated vapor of 0.3MPa, and coil heat exchanger is fixed in shell (1) by fixture.
7. flue gas ash removal as described in claim 1 takes off white integrated apparatus, it is characterised in that: gas inlet (2) and wet type are quiet
It is equipped with uniform board between electrical dust collector device (3), enables flue gas evenly into wet static dedusting device (3).
8. flue gas ash removal as described in claim 1 takes off white integrated apparatus, it is characterised in that: wet static dedusting device (3)
Several spray nozzles (9) are equipped between water separator (4), the water spraying direction of spray nozzle (9) is downward, quiet in wet type
When electrical dust collector device (3) power failure is not reruned, the bottom of regular spraying-rinsing anode tube (8), shell (1) has sewage draining exit
(10), sewage draining exit (10) and gas inlet (2) and exhaust gases passes are mutually isolated.
9. flue gas ash removal as described in claim 1 takes off white integrated apparatus, it is characterised in that: flue gas is cooling condensing unit (5)
Flusher is equipped between demister (6), which includes the Flushing nozzle that several are upwardly or downwardly arranged
(11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811225684.XA CN109078445A (en) | 2018-10-21 | 2018-10-21 | Flue gas ash removal takes off white integrated apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811225684.XA CN109078445A (en) | 2018-10-21 | 2018-10-21 | Flue gas ash removal takes off white integrated apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109078445A true CN109078445A (en) | 2018-12-25 |
Family
ID=64844010
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811225684.XA Pending CN109078445A (en) | 2018-10-21 | 2018-10-21 | Flue gas ash removal takes off white integrated apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109078445A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109772124A (en) * | 2019-03-27 | 2019-05-21 | 广东佳德环保科技有限公司 | A kind of flue gas desulfurization and denitrification takes off white equipment |
| CN109876589A (en) * | 2019-03-15 | 2019-06-14 | 海宁马桥大都市热电有限公司 | The system and method for white purified treatment are taken off for Hazards in Power Plant flue gas |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104190544A (en) * | 2014-09-17 | 2014-12-10 | 上海交通大学 | Dismountable smoke wet type electrostatic dust and fog removing device and application |
| CN104208996A (en) * | 2014-06-16 | 2014-12-17 | 中电投远达环保工程有限公司 | Desulfurizing and dedusting apparatus |
| CN105561726A (en) * | 2016-02-03 | 2016-05-11 | 江门市同力环保科技有限公司 | Effect improving type wet type electrostatic dust removal and mist removal device |
| CN105688582A (en) * | 2016-04-07 | 2016-06-22 | 国电环境保护研究院 | Condensation wet type electric compound flue gas purification process |
| CN107008098A (en) * | 2017-05-27 | 2017-08-04 | 河北远征环保科技有限公司 | Eliminate the device and removing method of fuel boiler flue gas hangover |
| CN206823458U (en) * | 2017-05-08 | 2018-01-02 | 浙江大学 | A kind of coal-burning power plant's energy-saving dedusting synergy cooperative intelligentization regulation and control remove white system |
| CN107617319A (en) * | 2017-11-10 | 2018-01-23 | 宿迁龙净环保科技有限公司 | A kind of ultra-clean environment protection treating island of coal-fired boiler tail gas |
| CN107970637A (en) * | 2017-12-29 | 2018-05-01 | 武汉龙净环保工程有限公司 | A kind of absorption tower and condensation receipts water dust removal method that water dust pelletizing system is received with condensation |
| CN108310794A (en) * | 2018-03-14 | 2018-07-24 | 红河绿地环保科技发展有限公司 | A method of remove smoke floss hole white haze steam |
| CN208905998U (en) * | 2018-10-21 | 2019-05-28 | 山东盛宝传热科技有限公司 | A kind of flue gas ash removal takes off white integrated apparatus |
-
2018
- 2018-10-21 CN CN201811225684.XA patent/CN109078445A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104208996A (en) * | 2014-06-16 | 2014-12-17 | 中电投远达环保工程有限公司 | Desulfurizing and dedusting apparatus |
| CN104190544A (en) * | 2014-09-17 | 2014-12-10 | 上海交通大学 | Dismountable smoke wet type electrostatic dust and fog removing device and application |
| CN105561726A (en) * | 2016-02-03 | 2016-05-11 | 江门市同力环保科技有限公司 | Effect improving type wet type electrostatic dust removal and mist removal device |
| CN105688582A (en) * | 2016-04-07 | 2016-06-22 | 国电环境保护研究院 | Condensation wet type electric compound flue gas purification process |
| CN206823458U (en) * | 2017-05-08 | 2018-01-02 | 浙江大学 | A kind of coal-burning power plant's energy-saving dedusting synergy cooperative intelligentization regulation and control remove white system |
| CN107008098A (en) * | 2017-05-27 | 2017-08-04 | 河北远征环保科技有限公司 | Eliminate the device and removing method of fuel boiler flue gas hangover |
| CN107617319A (en) * | 2017-11-10 | 2018-01-23 | 宿迁龙净环保科技有限公司 | A kind of ultra-clean environment protection treating island of coal-fired boiler tail gas |
| CN107970637A (en) * | 2017-12-29 | 2018-05-01 | 武汉龙净环保工程有限公司 | A kind of absorption tower and condensation receipts water dust removal method that water dust pelletizing system is received with condensation |
| CN108310794A (en) * | 2018-03-14 | 2018-07-24 | 红河绿地环保科技发展有限公司 | A method of remove smoke floss hole white haze steam |
| CN208905998U (en) * | 2018-10-21 | 2019-05-28 | 山东盛宝传热科技有限公司 | A kind of flue gas ash removal takes off white integrated apparatus |
Non-Patent Citations (3)
| Title |
|---|
| 中国石油天然气总公司: "石油地面工程设计手册", 31 October 1995, 石油大学出版社, pages: 711 - 712 * |
| 郑沛然: "炼钢设备与车间设计", 31 October 1996, 冶金工业出版社, pages: 51 - 53 * |
| 顾仁等: "冶金除尘手册", 30 June 1991, 冶金工业出版社, pages: 138 - 140 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109876589A (en) * | 2019-03-15 | 2019-06-14 | 海宁马桥大都市热电有限公司 | The system and method for white purified treatment are taken off for Hazards in Power Plant flue gas |
| CN109772124A (en) * | 2019-03-27 | 2019-05-21 | 广东佳德环保科技有限公司 | A kind of flue gas desulfurization and denitrification takes off white equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104226479B (en) | The high-efficient wet-type electric precipitation purifier and method of a kind of wet-method desulfurized fume | |
| US4284609A (en) | Condensation cleaning of particulate laden gases | |
| WO2016058141A1 (en) | Method and device for dedusting and desulphurizing flue gas | |
| US6726748B2 (en) | Method of converting a downflow/upflow wet flue gas desulfurization (WFGD) system to an upflow single-loop WFGD system | |
| CN205424963U (en) | Boiler flue gas purification system | |
| CN106268178B (en) | A kind of dedusting for wet desulfurization system-mist integrated apparatus and method | |
| CN206823458U (en) | A kind of coal-burning power plant's energy-saving dedusting synergy cooperative intelligentization regulation and control remove white system | |
| KR102387292B1 (en) | Exhaust gas treatment process system of after tenter added activated carbon filter and cyclone scrubber having rotary washing water supply means | |
| CN102172468A (en) | Three-pass dedusting devulcanizer | |
| CN105597483A (en) | Device and method for removing vapor dissolved particles by virtue of wet desulphurization exhaust gas cooling method | |
| CN109078445A (en) | Flue gas ash removal takes off white integrated apparatus | |
| CN109772124A (en) | A kind of flue gas desulfurization and denitrification takes off white equipment | |
| CN202289850U (en) | Smoke burning disposal system for sludge | |
| CN208905998U (en) | A kind of flue gas ash removal takes off white integrated apparatus | |
| CN211936330U (en) | High temperature pyrolysis incinerator tail gas electrostatic precipitator | |
| CN206131026U (en) | Industrial boiler flue gas processing system | |
| US5676715A (en) | Key advanced linear kinetic absorber system particulate arresting device | |
| CN210021654U (en) | Waste rubber desulfurization waste gas recovery processing device | |
| CN2305242Y (en) | Wet composite smoke purifier for boiler | |
| CN111363868A (en) | Steel slag heat treatment system and method | |
| CN209093063U (en) | A kind of coloured plume cancellation element of sintering flue gas | |
| CN201684533U (en) | Wet dust removal desulfurizing unit | |
| CN109513270A (en) | Supersonic speed fume-dehydrating degranulation object separator | |
| CN206121390U (en) | Wet -type dust collector | |
| CN214598041U (en) | Wet and hot dust-containing tail gas treatment device |
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 | ||
| CB02 | Change of applicant information |
Address after: 262100 northwest corner of the intersection of Jinshan street and Yanggan Road, Xin'an street, Anqiu City, Weifang City, Shandong Province Applicant after: SHANDONG SHENGBAO HEAT TRANSFER TECHNOLOGY Co.,Ltd. Address before: 262100 intersection of Xin'an street, Jinshan street and Yanggan Road, Anqiu City, Weifang City, Shandong Province Applicant before: SHANDONG SHENGBAO HEAT TRANSFER TECHNOLOGY Co.,Ltd. |
|
| CB02 | Change of applicant information |