CN106345217A - Boiler exhaust gas purifying device - Google Patents
Boiler exhaust gas purifying device Download PDFInfo
- Publication number
- CN106345217A CN106345217A CN201610909161.1A CN201610909161A CN106345217A CN 106345217 A CN106345217 A CN 106345217A CN 201610909161 A CN201610909161 A CN 201610909161A CN 106345217 A CN106345217 A CN 106345217A
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- Prior art keywords
- pipeline
- adsorber
- spray chamber
- communicated
- casing
- Prior art date
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- 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
-
- 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
- B01D50/60—Combinations of devices covered by groups B01D46/00 and B01D47/00
-
- 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
- B01D53/02—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 adsorption, e.g. preparative gas chromatography
- B01D53/04—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 adsorption, e.g. preparative gas chromatography with stationary adsorbents
-
- 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
- B01D53/14—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 absorption
- B01D53/18—Absorbing units; Liquid distributors therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/04—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
- B01J20/048—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium containing phosphorus, e.g. phosphates, apatites, hydroxyapatites
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/06—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
- B01J20/08—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04 comprising aluminium oxide or hydroxide; comprising bauxite
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28033—Membrane, sheet, cloth, pad, lamellar or mat
-
- 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)
- Analytical Chemistry (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention provides a boiler exhaust gas purifying device, comprising a case body, an air inlet pipe arranged at the top of the case body, a first pipeline communicated with the air inlet pipe, a desulfurizing pump communicated with the first pipeline, a second pipeline communicated with the desulfurizing pump, a dilute nitric acid sprinkling chamber communicated with the second pipeline, a third pipeline communicated with the dilute nitric acid sprinkling chamber, an adsorber communicated with the third pipeline, a fourth pipeline communicated with the adsorber, a clear water sprinkling chamber communicated with the fourth pipeline, and a gas outlet pipe communicated with the clear water sprinkling chamber; an active carbon filter screen, an HEPA filter screen and a ceramic filter screen are sequentially arranged along the gas inlet direction in the adsorber; two air deflectors opposite up and down are arranged on one side of the adsorber close to the third pipeline; and the distance between the two air deflectors increases gradually in the gas inlet direction. The boiler exhaust gas purifying device is simple in structure, low in manufacturing cost and suitable for use for boiler equipment in enterprises on middle and small scales.
Description
Technical field
The present invention relates to boiler waste gas purification technical field, more particularly, to a kind of boiler waste gas purification device.
Background technology
During boiler work, waste gas is discharged by chimney, wherein contain a large amount of dust and other harmful gass, particularly exist
When burning insufficient, the billowing black smoke of discharge is the insufficient coke solids granule of burning.These contain a large amount of dust,
If the gas of grain is directly discharged in environment, can environment be caused greatly endanger, more can cause the various breathing of the mankind
Disease.
People employ various off-gas cleaning equipments to process boiler waste gas, and existing boiler waste gas purification device is usual
Complex structure, cost is high, is not suitable for the boiler plant of some medium and small enterprises, is not easy to penetration and promotion.Therefore, it is necessary to carry
For a kind of boiler waste gas purification device, to solve the above problems.
In addition, as the vitals of waste gas purification, effect played in cleaning equipment for the adsorber is particularly significant.Existing
Adsorber material single, one-component garbage can only be filtered it is therefore desirable to improve.
Content of the invention
The technical problem to be solved in the present invention is to provide a kind of boiler waste gas purification device, to solve existing boiler waste gas
The problems of purifier.Meanwhile, present invention also offers a kind of activated charcoal strainer moulding material and preparation method thereof.
Meanwhile, present invention also offers a kind of adsorber of boiler waste gas purification device, the adsorber of boiler waste gas purification device
Activated charcoal strainer manufacture method.
For solving above-mentioned technical problem, the technical solution used in the present invention is:
A kind of boiler waste gas purification device, comprising: casing, the air inlet pipe located at described casing top and described air inlet pipe
Second pipe that first pipeline and the desulfurization pump of described first pipeline communication of connection is connected with described desulfurization pump and described the
The 3rd pipeline and described 3rd pipeline communication that the dust technology spray chamber of two pipeline communications is connected with described dust technology spray chamber
The 4th pipeline that connects with described adsorber of adsorber and the clear water spray chamber of described 4th pipeline communication and described clear water
The escape pipe of spray chamber connection；
Described wall box is provided with the first row QI KOU connecting with described desulfurization pump；Described wall box is provided with dilute with described
The second exhaust port of nitric acid spray chamber connection, opposite side wall is provided with the first leakage fluid dram connecting with described dust technology spray chamber；Institute
State wall box and be provided with the 3rd air vent connecting with described adsorber；Described wall box is provided with described clear water spray chamber even
The second logical leakage fluid dram；It is sequentially provided with activated charcoal strainer, hepa drainage screen and pottery along airintake direction inside described adsorber
Drainage screen；Described adsorber is provided with two deflectors opposing upper and lower, described two water conservancy diversion near the side of described 3rd pipeline
The distance between plate is gradually increased on airintake direction.
Described activated charcoal strainer, hepa drainage screen and foam ceramic filter are bonded to each other.
Described box bottom is provided with universal wheel.
Activated charcoal strainer moulding material, is made up of the raw material of following weight portion:
50 parts of activated carbon, 10 parts of glass fibre, 5 parts of aluminium oxide, 5 parts of calcium hypophosphite, 3 parts of peonol, 10 parts of glycerol.
The preparation method of activated charcoal strainer moulding material, comprises the steps:
1. in reaction vessel, add 25 parts of activated carbon, 5 parts of glass fibre, 5 parts of calcium hypophosphite and 10 parts of glycerol, in
1000 revs/min of rotating speed, stir 20 minutes at a temperature of 50 DEG C；
2., 25 parts of activated carbon and 5 parts of aluminium oxide are added to reaction vessel, in 1500 revs/min of rotating speeds, 35 DEG C of temperature
The lower stirring of degree 5 minutes；
3., 5 parts of glass fibre and 3 parts of peonol are added to reaction vessel, in 1250 revs/min of rotating speeds, 70 DEG C
At a temperature of stir 30 minutes, obtain mixed powder, i.e. activated charcoal strainer moulding material.
The adsorber of boiler waste gas purification device, along airintake direction be sequentially provided with activated charcoal strainer, hepa drainage screen and
Foam ceramic filter, activated charcoal strainer is made up of activated charcoal strainer moulding material.
The manufacture method of the activated charcoal strainer of the adsorber of boiler waste gas purification device, comprises the steps:
1., activated charcoal strainer moulding material is heated to molten condition, is sieved using 500 eye mesh screens；
2., molten state material is filled with processing mold, keeps 5 minutes under 10mpa pressure；
3., naturally cool to room temperature, the then demoulding obtains drainage screen stock；
4., put in heat-treatment furnace and process 30 minutes, treatment temperature is 200 DEG C, obtains activated charcoal strainer.
Advantage for present invention with effect is:
1), the kind boiler waste gas purification device of the present invention, comprising: casing, the air inlet pipe located at casing top and air inlet pipe
The second pipe that first pipeline of connection is connected with desulfurization pump with the desulfurization pump of the first pipeline communication is connected with second pipe
The 3rd pipeline that dust technology spray chamber is connected with dust technology spray chamber is connected with adsorber with the adsorber of the 3rd pipeline communication
The escape pipe that connects with clear water spray chamber with the clear water spray chamber of the 4th pipeline communication of the 4th pipeline；Wall box be provided with
The first row QI KOU of desulfurization pump connection；Wall box is provided with the second exhaust port connecting with dust technology spray chamber, and opposite side wall sets
There is the first leakage fluid dram connecting with dust technology spray chamber；Wall box is provided with the 3rd air vent connecting with adsorber；Case-side
Wall is provided with the second leakage fluid dram connecting with clear water spray chamber；Inside adsorber along airintake direction be sequentially provided with activated charcoal strainer,
Hepa drainage screen and foam ceramic filter；Adsorber is provided with two deflectors opposing upper and lower near the side of the 3rd pipeline, two
The distance between deflector is gradually increased on airintake direction；Structure is simple, low cost, is suitable for the pot of some medium and small enterprises
The use of furnace apparatus.
2), activated charcoal strainer moulding material and preparation method thereof, by reasonable selection raw material and proportioning, makes to be finally made
The service life of activated charcoal strainer significantly extended, and better mechanical property, bearing strength is higher.
3), the adsorber of boiler waste gas purification device, is designed by tertiary structure, so that the absorption property of adsorber is shown
Write lifting, to meet the absorption demand of the waste gas in boiler waste gas purification device.
4), the manufacture method of the activated charcoal strainer of the adsorber of boiler waste gas purification device, is processed by appropriate design
Technique, makes the drainage screen made, and mechanical load-bearing capability is strong, long service life, and product low cost meets the pot of medium and small enterprise
The use demand of furnace apparatus.
Brief description
The invention will be further described below in conjunction with the accompanying drawings:
Fig. 1 is the cross-sectional view of the boiler waste gas purification device of the present invention；
Fig. 2 is the structural representation of the adsorber of boiler waste gas purification device of the present invention.
In figure: casing 1, air inlet pipe 2, the first pipeline 3, desulfurization pump 4, second pipe 6, dust technology spray chamber 7, the 3rd pipeline
9th, adsorber 10, the 4th pipeline 14, clear water spray chamber 15, escape pipe 17, first row QI KOU 5, second exhaust port 8, the first discharge opeing
Mouth the 81, the 3rd air vent 13, the second leakage fluid dram 17, activated charcoal strainer 11, hepa drainage screen 110, foam ceramic filter 12, water conservancy diversion
Plate 120, universal wheel 18.
Specific embodiment
Embodiment 1
As shown in Figure 1 to Figure 2, the present invention provides a kind of boiler waste gas purification device, comprising: casing 1, push up located at casing 1
The desulfurization pump 4 that the first pipeline 3 that the air inlet pipe 2 in portion is connected with air inlet pipe 2 is connected with the first pipeline 3 is connected with desulfurization pump 4
The 3rd pipeline 9 and that the dust technology spray chamber 7 that second pipe 6 is connected with second pipe 6 is connected with dust technology spray chamber 7
The clear water spray chamber that the 4th pipeline 14 that the adsorber 10 of three pipeline 9 connection is connected with adsorber 10 is connected with the 4th pipeline 14
The escape pipe 17 that 15 are connected with clear water spray chamber 15, boiler waste gas can enter from air inlet pipe 2, is carried out at desulfurization by desulfurization pump 4
Reason, carries out denitration process by dust technology spray chamber 7 afterwards, carries out Filtration Adsorption by adsorber 10 afterwards, passes through clear afterwards
Water spray room 15 is carried out, and discharges the gas of cleaning eventually through escape pipe 17.
Further, casing 1 side wall is provided with the first row QI KOU 5 connecting with desulfurization pump 4, can discharge after desulfurization pump 4 desulfurization
Gas.Casing 1 side wall is provided with the second exhaust port 8 connecting with dust technology spray chamber 7, can discharge the gas through desulfurization and denitration
Body.Opposite side wall is provided with the first leakage fluid dram 81 connecting with dust technology spray chamber 7, for discharging the liquid in dust technology spray chamber 7
Body.Casing 1 side wall is provided with the 3rd air vent 13 connecting with adsorber 10, for discharging through desulfurization and denitration and Filtration Adsorption
Gas.Casing 1 side wall is provided with the second leakage fluid dram 17 connecting with clear water spray chamber 15, for discharging in clear water spray chamber 15
Liquid.It is sequentially provided with activated charcoal strainer 11, hepa drainage screen 110 and foam ceramic filter along airintake direction inside adsorber 10
12；Adsorber 10 is provided with two deflectors 120 opposing upper and lower near the side of the 3rd pipeline 9, between two deflectors 120
Distance is gradually increased on airintake direction, enters the gas within adsorber 10 and flows along deflector 120, with activated charcoal strainer
11st, hepa drainage screen 110 and foam ceramic filter 12 are fully contacted, and carry out Filtration Adsorption.In the present embodiment, activated charcoal strainer
11st, hepa drainage screen 110 and foam ceramic filter 12 are bonded to each other.Further, casing 1 bottom is provided with universal wheel 18, facilitates this
The movement of bright boiler waste gas purification device.
From above technical scheme, the boiler waste gas purification device of the present invention, structure is simple, low cost, is suitable for
The use of the boiler plant of medium and small enterprise.
Embodiment 2
Activated charcoal strainer moulding material, is made up of the raw material of following weight portion:
50 parts of activated carbon, 10 parts of glass fibre, 5 parts of aluminium oxide, 5 parts of calcium hypophosphite, 3 parts of peonol, 10 parts of glycerol.
The preparation method of activated charcoal strainer moulding material, comprises the steps:
1. in reaction vessel, add 25 parts of activated carbon, 5 parts of glass fibre, 5 parts of calcium hypophosphite and 10 parts of glycerol, in
1000 revs/min of rotating speed, stir 20 minutes at a temperature of 50 DEG C；
2., 25 parts of activated carbon and 5 parts of aluminium oxide are added to reaction vessel, in 1500 revs/min of rotating speeds, 35 DEG C of temperature
The lower stirring of degree 5 minutes；
3., 5 parts of glass fibre and 3 parts of peonol are added to reaction vessel, in 1250 revs/min of rotating speeds, 70 DEG C
At a temperature of stir 30 minutes, obtain mixed powder, i.e. activated charcoal strainer moulding material.
Embodiment 3
The adsorber of boiler waste gas purification device, along airintake direction be sequentially provided with activated charcoal strainer, hepa drainage screen and
Foam ceramic filter, activated charcoal strainer is made up of activated charcoal strainer moulding material.
The manufacture method of the activated charcoal strainer of the adsorber of boiler waste gas purification device, comprises the steps:
1., activated charcoal strainer moulding material (prepared by embodiment 2) is heated to molten condition, using 500 eye mesh screen mistakes
Sieve；
2., molten state material is filled with processing mold, keeps 5 minutes under 10mpa pressure；
3., naturally cool to room temperature, the then demoulding obtains drainage screen stock；
4., put in heat-treatment furnace and process 30 minutes, treatment temperature is 200 DEG C, obtains activated charcoal strainer.
The present invention is not limited to above-described embodiment, and embodiment is exemplary it is intended to be used for explaining the present invention, and can not
It is interpreted as limitation of the present invention.
Claims (3)
1. a kind of boiler waste gas purification device is it is characterised in that include: casing (1), the air inlet located at described casing (1) top
Desulfurization pump (4) and institute that the first pipeline (3) that pipe (2) is connected with described air inlet pipe (2) is connected with described first pipeline (3)
State the dust technology spray chamber (7) that the second pipe (6) that desulfurization pump (4) connects connected with described second pipe (6) dilute with described
Adsorber (10) and described adsorber that the 3rd pipeline (9) that nitric acid spray chamber (7) connects is connected with described 3rd pipeline (9)
(10) clear water spray chamber (15) and described clear water spray that the 4th pipeline (14) connecting is connected with described 4th pipeline (14)
The escape pipe (17) that room (15) connects；
Described casing (1) side wall is provided with the first row QI KOU (5) connecting with described desulfurization pump (4)；Described casing (1) side wall is provided with
The second exhaust port (8) connecting with described dust technology spray chamber (7), opposite side wall is provided with described dust technology spray chamber (7) even
Logical the first leakage fluid dram (81)；Described casing (1) side wall is provided with the 3rd air vent (13) connecting with described adsorber (10)；Institute
State casing (1) side wall and be provided with the second leakage fluid dram (17) connecting with described clear water spray chamber (15)；Described adsorber (10) is internal
It is sequentially provided with activated charcoal strainer (11), hepa drainage screen (110) and foam ceramic filter (12) along airintake direction；Described adsorber
(10) it is provided with two deflectors (120) opposing upper and lower, described two deflectors near the side of described 3rd pipeline (9)
The distance between (120) it is gradually increased on airintake direction.
2. boiler waste gas purification device according to claim 1 it is characterised in that described activated charcoal strainer (11),
Hepa drainage screen (110) and foam ceramic filter (12) are bonded to each other.
3. boiler waste gas purification device according to claim 2 it is characterised in that described casing (1) bottom be provided with universal
Wheel (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610909161.1A CN106345217A (en) | 2016-10-18 | 2016-10-18 | Boiler exhaust gas purifying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610909161.1A CN106345217A (en) | 2016-10-18 | 2016-10-18 | Boiler exhaust gas purifying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106345217A true CN106345217A (en) | 2017-01-25 |
Family
ID=57866439
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610909161.1A Withdrawn CN106345217A (en) | 2016-10-18 | 2016-10-18 | Boiler exhaust gas purifying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106345217A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107281893A (en) * | 2017-08-11 | 2017-10-24 | 合肥达科环保科技有限公司 | A kind of processing method of the three-level purifying tube of boiler waste gas purification device |
| CN107413131A (en) * | 2017-08-11 | 2017-12-01 | 合肥达科环保科技有限公司 | A kind of furniture drying boiler waste gas purification device |
| CN107469549A (en) * | 2017-08-11 | 2017-12-15 | 合肥达科环保科技有限公司 | A kind of three-level purifying tube of boiler waste gas purification device |
| CN108636061A (en) * | 2018-04-17 | 2018-10-12 | 南安市创培电子科技有限公司 | A kind of high effective desulphurization device of boiler waste gas |
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| US20060029532A1 (en) * | 2004-08-03 | 2006-02-09 | Breen Bernard P | Dry adsorption of oxidized mercury in flue gas |
| CN204213942U (en) * | 2014-10-30 | 2015-03-18 | 青岛华武橡塑有限公司 | A kind of boiler waste gas purification device |
| CN105032065A (en) * | 2015-06-06 | 2015-11-11 | 杭州笨鸟环保科技有限公司 | Active carbon filter screen and preparation method thereof |
| CN204996283U (en) * | 2015-09-18 | 2016-01-27 | 哈尔滨市金京锅炉有限公司 | Boiler exhaust -gas treatment apparatus |
| CN105944460A (en) * | 2016-07-08 | 2016-09-21 | 黄斌 | Waste gas purifying device for boiler |
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2016
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| CN204213942U (en) * | 2014-10-30 | 2015-03-18 | 青岛华武橡塑有限公司 | A kind of boiler waste gas purification device |
| CN105032065A (en) * | 2015-06-06 | 2015-11-11 | 杭州笨鸟环保科技有限公司 | Active carbon filter screen and preparation method thereof |
| CN204996283U (en) * | 2015-09-18 | 2016-01-27 | 哈尔滨市金京锅炉有限公司 | Boiler exhaust -gas treatment apparatus |
| CN105944460A (en) * | 2016-07-08 | 2016-09-21 | 黄斌 | Waste gas purifying device for boiler |
Non-Patent Citations (1)
| Title |
|---|
| 许钦一: "高比表面积成型活性炭的制备及其性能研究", 《中国优秀硕士学位论文全文数据库工程科技I辑（月刊）》 * |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107281893A (en) * | 2017-08-11 | 2017-10-24 | 合肥达科环保科技有限公司 | A kind of processing method of the three-level purifying tube of boiler waste gas purification device |
| CN107413131A (en) * | 2017-08-11 | 2017-12-01 | 合肥达科环保科技有限公司 | A kind of furniture drying boiler waste gas purification device |
| CN107469549A (en) * | 2017-08-11 | 2017-12-15 | 合肥达科环保科技有限公司 | A kind of three-level purifying tube of boiler waste gas purification device |
| CN108636061A (en) * | 2018-04-17 | 2018-10-12 | 南安市创培电子科技有限公司 | A kind of high effective desulphurization device of boiler waste gas |
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Application publication date: 20170125 |
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| WW01 | Invention patent application withdrawn after publication |