CN106731304A - A kind of glass melting kiln waste processing equipment - Google Patents
A kind of glass melting kiln waste processing equipment Download PDFInfo
- Publication number
- CN106731304A CN106731304A CN201611177532.8A CN201611177532A CN106731304A CN 106731304 A CN106731304 A CN 106731304A CN 201611177532 A CN201611177532 A CN 201611177532A CN 106731304 A CN106731304 A CN 106731304A
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- denitration
- cooling
- processing equipment
- waste processing
- room
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
- B01D46/12—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces in multiple arrangements
-
- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
- B01D53/50—Sulfur oxides
- B01D53/501—Sulfur oxides by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound
- B01D53/502—Sulfur oxides by treating the gases with a solution or a suspension of an alkali or earth-alkali or ammonium compound characterised by a specific solution or suspension
-
- 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
- B01D53/54—Nitrogen compounds
- B01D53/56—Nitrogen oxides
-
- 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
- B01D53/81—Solid phase processes
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- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/60—Inorganic bases or salts
- B01D2251/606—Carbonates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/60—Inorganic bases or salts
- B01D2251/608—Sulfates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
-
- 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
- B01D2258/0241—Other waste gases from glass manufacture plants
Abstract
The invention discloses a kind of glass melting kiln waste processing equipment, including glass melter, cooling, desulfurizing room, denitration chamber, adsorption layer, the glass melter connection cooling, desulfurizing room, cooling, desulfurizing is provided with screen pack in room, screen pack top is provided with liquid outlet, cooling, desulfurizing room is connected with denitration chamber by bifurcated passage, the other end of bifurcated passage connects 4 air admission holes of denitration chamber, denitration chamber side is provided with blade, blade is close to denitration chamber interior walls, through hole is provided with the middle of blade, rotating shaft axis are identical to through hole centre distance with rotating shaft axis to air admission hole centre distance, rotary shaft other end connection denitration cylinder, denitration cylinder side is provided with taphole, denitration chamber outlet connects chimney by adsorption layer, dedusting of the present invention, desulfurization, denitration efficiency is high, stable and reliable operation, take up an area small, operating cost is low.
Description
Technical field
The invention belongs to waste gas treatment equipment technical field, and in particular to a kind of glass melting kiln waste processing equipment.
Background technology
A large amount of dusty gas, wherein major pollutants can be given off after plate glass manufacturing enterprise, glass melter work
Be flue dust, SO2 and Nox, smog discharge temperature be up to 350-500 DEG C, NOx concentration >=2000mg/Nm3, SO2 concentration >=
2000mg/Nm3, dust concentration >=20g/Nm3, and viscosity very big, high corrosiveness, these pollutants can cause air dirty
The environmental problems such as dye, acid rain, greenhouse effects, comprehensive regulation difficulty is very big, and national environmental protection portion has promulgated《Flat glass industry
Atmosphere pollutants emission standardses GB26453-2011》, therefore the waste gas pollution control and treatment of glass melter production needs lasting development.At present
The waste gas treatment equipment majority operation conditions of implementation are poor, and being difficult to of having reaches standard requirement, some dedustings, denitration, desulfurization point
Drive row into, investment is big, floor space is big, some fluctuations of service, it is necessary to ceaselessly debug, glass melter air contaminant treatment
Task remains unchanged abnormal arduous, it is necessary to researcher continues to capture difficulty.
The content of the invention
To solve the above problems, the invention discloses a kind of glass melting kiln waste processing equipment, dedusting, desulphurization and denitration effect
Rate is high, stable and reliable operation, and occupation of land is small, and operating cost is low.
To reach above-mentioned purpose, technical scheme is as follows：
A kind of glass melting kiln waste processing equipment, it is characterised in that：Including glass melter, cooling, desulfurizing room, denitration chamber, absorption
Layer, the glass melter connection cooling, desulfurizing room, is provided with least 4 floor screen pack, screen pack being vertically arranged in cooling, desulfurizing room
Top is provided with liquid outlet, and the liquid outlet connection desulfurizing agent locker room is provided with outlet one, cooling, desulfurizing room below cooling, desulfurizing room
Connected by bifurcated passage with denitration chamber, the gas outlet of one end connection cooling, desulfurizing room of the bifurcated passage, bifurcated passage
The air admission hole of other end connection denitration chamber, the quantity of the air admission hole at least 4, denitration chamber side is provided with motor, motor connection
Rotary shaft, rotary shaft side is provided with blade, and blade is close to denitration chamber interior walls, is provided with through hole in the middle of blade, and rotating shaft axis are to entering
Stomata centre distance is identical to through hole centre distance with rotating shaft axis, rotary shaft other end connection denitration cylinder, denitration cylinder side
Taphole is provided with, the opposite side of denitration cylinder is provided with connecting hole, and denitration chamber outside is provided with liquid feeding tower, and connection hole is connected by bearing
Logical liquid feeding tower, denitration chamber outlet connects chimney by adsorption layer, and denitration chamber lower section is provided with outlet two, the cooling, desulfurizing room, takes off
Nitre is provided with anticorrosive coat in room.
Used as a modification of the present invention, the bifurcated passage is provided with thermometer.
Used as a modification of the present invention, the mesh diameter of the screen pack is 0.3-0.5mm.
As a modification of the present invention, a diameter of 0.2-0.3mm of the taphole.
Used as a modification of the present invention, the anticorrosive coat is enamel layer.
Used as a modification of the present invention, the thickness of the anticorrosive coat is 1.5mm.
Used as a modification of the present invention, the adsorption layer is 3 layers.
Used as a modification of the present invention, the adsorption layer is drawer type adsorption layer.
Used as a modification of the present invention, the motor is buncher.
Used as a modification of the present invention, the denitration chamber side is provided with access hole.
The beneficial effects of the invention are as follows：
A kind of glass melting kiln waste processing equipment of the present invention, flue gas enters cooling, desulfurizing room from glass melter, utilizes
Filter screen and basic sulfate aluminum solutions（Desulfurizing agent）To high-temp waste gas simultaneously lowered the temperature, dedusting, desulfurization, high working efficiency, then
Flue gas enters denitration chamber from air admission hole, can enter when flue gas only has air admission hole to be overlapped with through hole, is rotated at a high speed after
Blade be divided into a silk, and and then blade forms eddy flow, the CaCO3 solution in liquid feeding tower（Denitrfying agent）By compressing mist
Change and sprayed from taphole, the cut smoke reaction with synchronous rotary, denitration efficiency is high, speed is fast, mass transfer velocity is fast, most
By being discharged after wood charcoal adsorption, adsorption layer can dehumidify and inhale taste flue gas, and dust removal efficiency more than 99%, desulfurization degree more than 94% takes off afterwards
Nitre rate more than 87%, stable and reliable operation is taken up an area and reduces 40-60%, and small investment, exhaust-gas treatment speed improves 15%, operating cost
It is low.
Brief description of the drawings
Fig. 1 is structural representation of the invention.
Fig. 2 is blade schematic diagram of the present invention.
Reference numerals list：
1st, glass melter, 2, cooling, desulfurizing room, 3, denitration chamber, 4, adsorption layer, 5, screen pack, 6, liquid outlet, 7, desulfurizing agent storage
Room, 8, outlet one, 9, bifurcated passage, 10, air admission hole, 11, motor, 12, rotary shaft, 13, blade, 14, through hole, 15, denitration cylinder,
16th, taphole, 17, liquid feeding tower, 18, access hole, 19, chimney, 20, outlet two, 21, thermometer.
Specific embodiment
With reference to the accompanying drawings and detailed description, the present invention is furture elucidated, it should be understood that following specific embodiments are only
For illustrating the present invention rather than limitation the scope of the present invention.It should be noted that the word " preceding " for being used in description below,
" afterwards ", "left", "right", "up" and "down" refer to the direction in accompanying drawing, and word " interior " and " outward " refer respectively to direction or remote
From the direction of particular elements geometric center.
As illustrated, a kind of glass melting kiln waste processing equipment of the present invention, including glass melter 1, cooling, desulfurizing
Room 2, denitration chamber 3, adsorption layer 4, the connection cooling, desulfurizing of the glass melter 1 room 2, are provided with what is be vertically arranged in cooling, desulfurizing room 2
At least 4 layers screen pack 5, screen pack top is provided with liquid outlet 6, the connection desulfurizing agent of the liquid outlet 6 locker room 7, cooling, desulfurizing room 2
Lower section is provided with outlet 1, and cooling, desulfurizing room 2 is connected with denitration chamber 3 by bifurcated passage 9, one end connection of the bifurcated passage 9
The gas outlet of cooling, desulfurizing room, the other end of bifurcated passage 9 connects the air admission hole 10 of denitration chamber, and the quantity of the air admission hole 10 is extremely
Few 4, denitration chamber side is provided with motor 11, and the connection rotary shaft 12 of motor 11, the side of rotary shaft 12 is provided with blade 13, and blade 13 is tight
Patch denitration chamber interior walls, are provided with through hole 14, the axis of rotary shaft 12 to the centre distance of air admission hole 10 and the axle of rotary shaft 12 in the middle of blade 13
Line is identical to the centre distance of through hole 14, rotary shaft other end connection denitration cylinder 15, and 15 sides of denitration cylinder are provided with taphole 16, take off
The opposite side of nitre cylinder 15 is provided with connecting hole, and denitration chamber outside is provided with liquid feeding tower 17, and connection hole connects liquid feeding tower 17 by bearing,
The outlet of denitration chamber 3 connects chimney 19 by adsorption layer 4, and the lower section of denitration chamber 3 is provided with outlet 2 20, the cooling, desulfurizing room 2, denitration
Anticorrosive coat is provided with room 3.
A kind of glass melting kiln waste processing equipment of the present invention, flue gas enters cooling, desulfurizing room from glass melter,
Lowered the temperature simultaneously in cooling, desulfurizing room 2, dedusting, desulfurization, be divided into one subsequently into the blade rotated at a high speed after denitration chamber 3
Silk silk, quick denitration is discharged, dedusting, desulphurization and denitration efficiency high, stable and reliable operation after eventually passing absorption, takes up an area small, throwing
Money is few, and exhaust-gas treatment speed is improved, and operating cost is low.
The present invention is provided with thermometer 21 on the bifurcated passage 9, can at any time monitor the flue gas temperature into denitration chamber 3
Degree.
The mesh diameter of screen pack of the present invention 5 is 0.3-0.5mm, by multiple filtration, can be by below 0.5mm's
Particle is all intercepted, and screen pack top constantly sprays desulfurizing agent, can either desulfurization, can lower the temperature again, and can be by mistake
The particle that filter screen is intercepted down washes away, and supplements normal filter capacity.
As a modification of the present invention, a diameter of 0.2-0.3mm of the taphole 16.
Anticorrosive coat of the present invention is enamel layer, corrosion-resistant, and high lubrication is not glued, and has good anti-aging endurance, uses the longevity
Life length, the thickness of anticorrosive coat is 1.5mm.
Adsorption layer of the present invention 4 is 3 layers, drawer type adsorption layer, can individually extract cleaning out and change, simple and practical.
Motor of the present invention 11 is buncher, can carry out speed adjustment according to the concentration of fume emission.
The present invention is provided with access hole 18 in the cooling, desulfurizing room 2, the side of denitration chamber 3, easy to maintenance.
Technological means disclosed in the present invention program is not limited only to the technological means disclosed in above-mentioned implementation method, also includes
Constituted technical scheme is combined by above technical characteristic.
Claims (10)
1. a kind of glass melting kiln waste processing equipment, it is characterised in that：Including glass melter, cooling, desulfurizing room, denitration chamber, absorption
Layer, the glass melter connection cooling, desulfurizing room, is provided with least 4 floor screen pack, screen pack being vertically arranged in cooling, desulfurizing room
Top is provided with liquid outlet, and the liquid outlet connection desulfurizing agent locker room is provided with outlet one, cooling, desulfurizing room below cooling, desulfurizing room
Connected by bifurcated passage with denitration chamber, the gas outlet of one end connection cooling, desulfurizing room of the bifurcated passage, bifurcated passage
The air admission hole of other end connection denitration chamber, the quantity of the air admission hole at least 4, denitration chamber side is provided with motor, motor connection
Rotary shaft, rotary shaft side is provided with blade, and blade is close to denitration chamber interior walls, is provided with through hole in the middle of blade, and rotating shaft axis are to entering
Stomata centre distance is identical to through hole centre distance with rotating shaft axis, rotary shaft other end connection denitration cylinder, denitration cylinder side
Taphole is provided with, the opposite side of denitration cylinder is provided with connecting hole, and denitration chamber outside is provided with liquid feeding tower, and connection hole is connected by bearing
Logical liquid feeding tower, denitration chamber outlet connects chimney by adsorption layer, and denitration chamber lower section is provided with outlet two, the cooling, desulfurizing room, takes off
Nitre is provided with anticorrosive coat in room.
2. a kind of glass melting kiln waste processing equipment according to claim 1, it is characterised in that：Set on the bifurcated passage
There is thermometer.
3. a kind of glass melting kiln waste processing equipment according to claim 1, it is characterised in that：The mesh of the screen pack
A diameter of 0.3-0.5mm.
4. a kind of glass melting kiln waste processing equipment according to claim 1, it is characterised in that：The taphole it is straight
Footpath is 0.2-0.3mm.
5. a kind of glass melting kiln waste processing equipment according to claim 1, it is characterised in that：The anticorrosive coat is enamel
Layer.
6. a kind of glass melting kiln waste processing equipment according to claim 5, it is characterised in that：The thickness of the anticorrosive coat
It is 1.5mm.
7. a kind of glass melting kiln waste processing equipment according to claim 1, it is characterised in that：The adsorption layer is 3 layers.
8. a kind of glass melting kiln waste processing equipment according to claim 1, it is characterised in that：The adsorption layer is drawer
Formula adsorption layer.
9. a kind of glass melting kiln waste processing equipment according to claim 1, it is characterised in that：The motor is speed governing electricity
Machine.
10. a kind of glass melting kiln waste processing equipment according to claim 1, it is characterised in that：The denitration chamber side
It is provided with access hole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611177532.8A CN106731304B (en) | 2016-12-19 | 2016-12-19 | A kind of glass melting kiln waste processing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611177532.8A CN106731304B (en) | 2016-12-19 | 2016-12-19 | A kind of glass melting kiln waste processing equipment |
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| Publication Number | Publication Date |
|---|---|
| CN106731304A true CN106731304A (en) | 2017-05-31 |
| CN106731304B CN106731304B (en) | 2018-01-30 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201611177532.8A Active CN106731304B (en) | 2016-12-19 | 2016-12-19 | A kind of glass melting kiln waste processing equipment |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107261792A (en) * | 2017-06-30 | 2017-10-20 | 南京律智诚专利技术开发有限公司 | A kind of inexpensive denitrating flue gas dust arrester |
| CN108744923A (en) * | 2018-07-20 | 2018-11-06 | 江苏安纳泰环保科技有限公司 | A kind of desulphurization denitration high efficiency spray wash mill |
| CN108744909A (en) * | 2018-07-19 | 2018-11-06 | 江苏安纳泰环保科技有限公司 | A kind of boiler flue gas desulfurization denitrification apparatus |
| CN108889101A (en) * | 2018-07-19 | 2018-11-27 | 江苏安纳泰环保科技有限公司 | A kind of flue gas purification device based on fluidized bed |
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| EP0310830A1 (en) * | 1987-10-09 | 1989-04-12 | Thyssen Industrie Ag | Venturi-cooler for a gas desulfuration plant |
| CN201997251U (en) * | 2010-12-31 | 2011-10-05 | 龙波 | Screw type movable liquid-fog smoke prevention, dust control, desulfuration and denitration absorption unit |
| CN204073759U (en) * | 2014-09-17 | 2015-01-07 | 陕西理工学院 | A kind of flue-gas dust-removing and desulfurization denitrification integrated device |
| CN104307311A (en) * | 2014-10-16 | 2015-01-28 | 太仓东能环保设备有限公司 | Fast desulfuration and dust removal device with multiple cavities |
| CN204710086U (en) * | 2015-04-29 | 2015-10-21 | 中起重工（大连）有限公司 | A kind of flue gas desulfur device |
-
2016
- 2016-12-19 CN CN201611177532.8A patent/CN106731304B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0310830A1 (en) * | 1987-10-09 | 1989-04-12 | Thyssen Industrie Ag | Venturi-cooler for a gas desulfuration plant |
| CN201997251U (en) * | 2010-12-31 | 2011-10-05 | 龙波 | Screw type movable liquid-fog smoke prevention, dust control, desulfuration and denitration absorption unit |
| CN204073759U (en) * | 2014-09-17 | 2015-01-07 | 陕西理工学院 | A kind of flue-gas dust-removing and desulfurization denitrification integrated device |
| CN104307311A (en) * | 2014-10-16 | 2015-01-28 | 太仓东能环保设备有限公司 | Fast desulfuration and dust removal device with multiple cavities |
| CN204710086U (en) * | 2015-04-29 | 2015-10-21 | 中起重工（大连）有限公司 | A kind of flue gas desulfur device |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107261792A (en) * | 2017-06-30 | 2017-10-20 | 南京律智诚专利技术开发有限公司 | A kind of inexpensive denitrating flue gas dust arrester |
| CN108744909A (en) * | 2018-07-19 | 2018-11-06 | 江苏安纳泰环保科技有限公司 | A kind of boiler flue gas desulfurization denitrification apparatus |
| CN108889101A (en) * | 2018-07-19 | 2018-11-27 | 江苏安纳泰环保科技有限公司 | A kind of flue gas purification device based on fluidized bed |
| CN108744909B (en) * | 2018-07-19 | 2021-04-27 | 江苏安纳泰环保科技有限公司 | Boiler flue gas desulfurization and denitrification device |
| CN108744923A (en) * | 2018-07-20 | 2018-11-06 | 江苏安纳泰环保科技有限公司 | A kind of desulphurization denitration high efficiency spray wash mill |
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| Publication number | Publication date |
|---|---|
| CN106731304B (en) | 2018-01-30 |
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Address after: 224005 No. 8 (28) Photovoltaic Road, Environmental Protection Industrial Park, Tinghu District, Yancheng City, Jiangsu Province Patentee after: China Building Materials Environmental Protection Research Institute (Jiangsu) Co., Ltd. Address before: 224051 No. 8 Photovoltaic Road, Environmental Protection Industrial Park, Tinghu District, Yancheng City, Jiangsu Province Patentee before: Jiangsu CNBM Environmental Protection Research Institute Co., Ltd. |
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