CN108339365A - A kind of device and method for controlling the discharge of chemical engineering industry exhaust gas - Google Patents
A kind of device and method for controlling the discharge of chemical engineering industry exhaust gas Download PDFInfo
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- CN108339365A CN108339365A CN201710054135.XA CN201710054135A CN108339365A CN 108339365 A CN108339365 A CN 108339365A CN 201710054135 A CN201710054135 A CN 201710054135A CN 108339365 A CN108339365 A CN 108339365A
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- 238000003889 chemical engineering Methods 0.000 title claims abstract description 27
- 238000000034 method Methods 0.000 title claims abstract description 10
- 239000000126 substance Substances 0.000 claims abstract description 67
- 239000002912 waste gas Substances 0.000 claims abstract description 67
- 239000007789 gas Substances 0.000 claims abstract description 64
- 238000010521 absorption reaction Methods 0.000 claims abstract description 43
- 239000000779 smoke Substances 0.000 claims abstract description 41
- 238000005057 refrigeration Methods 0.000 claims abstract description 37
- 239000002699 waste material Substances 0.000 claims abstract description 34
- 230000004087 circulation Effects 0.000 claims abstract description 23
- 239000007788 liquid Substances 0.000 claims abstract description 17
- 239000000428 dust Substances 0.000 claims abstract description 16
- 238000004064 recycling Methods 0.000 claims abstract description 14
- 239000002440 industrial waste Substances 0.000 claims abstract description 6
- 238000004519 manufacturing process Methods 0.000 claims abstract description 5
- 239000007787 solid Substances 0.000 claims abstract description 3
- 230000008676 import Effects 0.000 claims description 13
- 239000002893 slag Substances 0.000 claims description 13
- 239000000463 material Substances 0.000 claims description 11
- 238000001816 cooling Methods 0.000 claims description 7
- 238000005868 electrolysis reaction Methods 0.000 claims description 7
- 239000011435 rock Substances 0.000 claims description 5
- 238000001179 sorption measurement Methods 0.000 claims description 5
- 235000019738 Limestone Nutrition 0.000 claims description 4
- 230000005494 condensation Effects 0.000 claims description 4
- 238000009833 condensation Methods 0.000 claims description 4
- 239000006028 limestone Substances 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 230000002093 peripheral effect Effects 0.000 claims description 2
- 230000035755 proliferation Effects 0.000 claims description 2
- 239000003566 sealing material Substances 0.000 claims description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 claims 3
- 239000011707 mineral Substances 0.000 claims 3
- 235000019504 cigarettes Nutrition 0.000 claims 1
- 230000001276 controlling effect Effects 0.000 abstract description 6
- 239000005431 greenhouse gas Substances 0.000 abstract description 4
- 230000001105 regulatory effect Effects 0.000 abstract description 3
- 239000003570 air Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000002156 adsorbate Substances 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 230000032696 parturition Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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
- B01D53/002—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
- 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
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/20—Waste processing or separation
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Treating Waste Gases (AREA)
Abstract
A kind of device and method for controlling the discharge of chemical engineering industry exhaust gas, the device is after the industrial waste gas for generating chemical furnace captures smoke pipe capture by high-temp waste gas, air-introduced machine is pressed to deflect from high temperature, after being sent by high temperature smoke pipe in the ontology of reversion type refrigeration condensing tower adjacent thereto, high-temp waste gas is after refrigeration condenses, when temperature drop reduces to environment temperature, it is adsorbed in the region for sending smoke pipe to be sent into chemical emission absorption and control area by the low temperature of the condensing tower of intermediate precedence again, and regulated and controled by waste gas circulation control terminal, realize chemical engineering industry zero waste gas emission.Waste residue, waste material and the recycling dust generated when the industrial waste gas that chemical furnace generates liquefies in liquefaction electrolytic furnace, and liquid influent cools down in the pond in solid-state pond, is stored at solid object after being cooled.The present invention is conducive to control the discharge of greenhouse gases, and can eliminate chemical furnace waste residue, waste material caused by production process and recycle the secondary pollution of dust.
Description
Technical field
The invention belongs to the construction applications without discharge ground or underground storage, more particularly to a kind of for controlling chemical engineering industry
The device and method of exhaust gas discharge.
Background technology
CN205517107U discloses a kind of emission-control equipment, and the efferent duct of the utility model is used for will be defeated in exhaust gas centralized
Go out, by the condensation vapor liquid in exhaust gas when passing through condenser, and simultaneously removes the harmful substance in exhaust gas by condensation vapor
It goes, when being passed through gas washing spray chamber, the harmful substance in exhaust gas is further adsorbed by water jet, then passes through activated carbon adsorption
Chamber is discharged after being adsorbed by exhaust pipe, and the gas of discharge meets discharge standard.
Lower greenhouse gas emission, prevent climate change acceleration from being the huge challenge and suddenly wait making up that chemical engineering industry faces
Short slab.The object of the present invention is to provide a kind of methods of energy stability contorting chemical engineering industry exhaust gas discharge, chemical engineering industry exhaust gas
It is conveyed into storage cavern area, allows chemical engineering industry exhaust gas to completely cut off for a long time with ambient air, alleviates the concentration of greenhouse gases.
Invention content
The purpose of the present invention is to provide a kind of device and method for controlling the discharge of chemical engineering industry exhaust gas, this method is logical
The transmission of exhaust energy and the absorption of physics are crossed, chemical engineering industry waste exhaust gases and pollutant full dose are controlled in sorbing material,
There is electrolytic furnace in device.
The technical scheme is that：
A kind of device for controlling the discharge of chemical engineering industry exhaust gas, the exit setting high-temp waste gas of 1 exhaust gas of chemical furnace
Smoke pipe 2 is captured, the import for capturing smoke pipe 2 is connect with the waste gas outlet of chemical furnace 1, is pressed and is drawn in the outlet of capture smoke pipe 2 and high temperature
The air-vent of wind turbine connects；The exhaust outlet of air-introduced machine 3 is pressed to pass through high temperature smoke pipe 4 and one group of reversion type refrigeration condensing tower 5 in high temperature
The connection of import smoke pipe, one group of reversion type refrigeration condensing tower 5 simplifies work high-temp waste gas partial pressure for dropping；Reversion type refrigeration condensation
Tower 5 is connect by low temperature snorkel 6 with chemical emission absorption and control area 7, and exhaust gas is arranged in the end in chemical emission absorption and control area 7
Loop control terminal, the internal circulating load for adjusting chemical emission；In the adjacent setting liquefaction electrolytic furnace 9 of chemical furnace 1, for giving birth to
Waste residue waste material and recycling dust are produced, the outlet for the electrolytic furnace 9 that liquefies, which is captured by electrolysis furnace exhaust in smoke pipe 10 and high temperature, presses air inducing
The air-vent of machine 3 connects.
One group of reversion type refrigeration condensing tower 5 in the junction of draught fan system includes the reverse of left, center, right three
Formula refrigeration condensing tower 5,5 ontology of each reversion type refrigeration condensing tower is interior to be arranged moisture trap 11, and condensed exhaust gas passes through low
Warm snorkel 6 is sent to chemical emission absorption and control area 7；The high temperature at 5 top of reversion type refrigeration condensing tower of the arranged on left and right sides
The air inlet of exhaust gas is connect with high temperature smoke pipe 4, and outlet is connect with medium temperature exhaust gas inlet 12, the medium temperature exhaust gas inlet 12 connection
It is set to the lower part of intermediate reversion type refrigeration condensing tower 5；The air inlet pipe of the reversion type refrigeration condensing tower 5 of the centre with it is left,
The exhaust outlet connection of right reversion type refrigeration condensing tower 5, outlet flue are connect with low temperature snorkel 6.
The low temperature waste gas import 13 in the chemical emission absorption and control area 7 is connect with low temperature snorkel 6, and chemical emission is inhaled
It is arranged in the region of attached control zone 7 multiple successively by the chemical emission absorption and control room 14 of placed in series, the absorption backfill of material 15
In chemical emission absorption and control area 7, outside chemical emission absorption and control room 14；The low temperature waste gas import 13 and first
14 unicom of chemical emission absorption and control room, the inlet and outlet in absorption and control area, i.e. the last one chemical emission absorption and control room 14 are logical
Cross cross over pipe 16 and waste gas circulation control terminal unicom 8；Exhaust gas control is arranged in the inside of the waste gas circulation control terminal unicom 8
Terminal adsorption chamber 17 processed, exhaust gas is by being arranged 18 discharge of waste gas circulation outlet in 8 side of waste gas circulation control terminal unicom.Institute
The peripheral carrier for the waste gas circulation control terminal 8 stated is built up by the sealing material of non-proliferation.
The liquefaction electrolytic furnace 9 is located at the top in liquid cooling solid-state pond 23；Setting above the side of liquefaction electrolytic furnace 9
The feed inlet 19 of one waste residue waste material, one recycling dust feed inlet 20 of other side top setting, lower part is arranged an electrolysis and melts
Liquid outlet 21, top are arranged a high-temp waste gas and export 22, and high-temp waste gas outlet 22 captures smoke pipe 2 with high-temp waste gas and is connected to.
Absorption material 15 of the present invention is volcanic rock, lime stone, metallurgical industry slag, coal-fired industry slag, mine heat
Stove slag, preferred volcanic rock are the adsorbate of best chemical emission, and material backfill is in the absorption and control area of chemical emission and gives up
In the region of gas loop control terminal.
The method that control chemical engineering industry exhaust gas discharge is carried out using above-mentioned apparatus, specially：The Industry Waste that chemical furnace 1 generates
Gas is captured by high-temp waste gas after smoke pipe 2 captures, and is sent by high temperature smoke pipe 4 after being pressed air-introduced machine 3 to deflect from high temperature adjacent thereto
After in the ontology of reversion type refrigeration condensing tower 5, high-temp waste gas is after refrigeration condenses, and the partial pressure of its coefficient of expansion reduces, height
When the temperature drop of warm exhaust gas reduces to environment temperature, then send smoke pipe 6 to be sent into chemical emission by the low temperature of the condensing tower 5 of intermediate precedence and inhale
The region of attached control zone 7 is adsorbed, and is regulated and controled by waste gas circulation control terminal 8, realizes chemical engineering industry zero waste gas emission.Chemical industry
Waste residue, waste material and the recycling dust generated when the industrial waste gas that stove 1 generates is under the working condition of liquefaction electrolytic furnace 9 by rapid liquid
Change, liquid under the water conservancy diversion of the liquid outlet 21 of liquefaction electrolytic furnace 9 in the pond in influent cooling solid-state pond 23, after being cooled at
Gu object is stored, eliminates chemical furnace 1 waste residue, waste material caused by production process and recycle the secondary pollution of dust.
The following of the present invention has the beneficial effect that：The present invention is conducive to control the discharge of greenhouse gases, and can eliminate chemical industry
Stove waste residue, waste material caused by production process and the secondary pollution for recycling dust, are conducive to the existence of the mankind far from chemical industry work
Industry, heavy metal pollution environment.
Description of the drawings
Fig. 1 is the device of the invention structure chart；
Fig. 2 is the structure chart of high-temp waste gas reversion type refrigeration condensing tower of the present invention；
Fig. 3 is the plane cut-away view in chemical emission absorption and control of the present invention area；
Fig. 4 is liquefaction electrolytic furnace structure chart of the present invention；
In figure：1 chemical furnace, 2 capture smoke pipes, press air-introduced machine, 4 high temperature smoke pipes in 3 high temperature, and 5 reversion types freeze condensing tower, and 6
Low temperature snorkel, 7 chemical emission absorption and control areas, 8 waste gas circulation control terminals, 9 liquefaction electrolytic furnaces, 10 electrolysis furnace exhausts capture
Smoke pipe, 11 moisture traps, 12 medium temperature exhaust gas inlets, 13 low temperature waste gas imports, 14 chemical emission absorption and control rooms, 15 adsorbates
Material, 16 cross over pipes, 17 exhaust gas control terminal adsorption chambers, 18 waste gas circulations outlet, 19 waste residue waste feedstock mouths, 20 recycling dust into
Material mouth, 21 electrolysis tapholes, the outlet of 22 high-temp waste gas, 23 liquid cool down solid-state pond.
Specific implementation mode
Below by way of specific implementation mode, the invention will be further described.
A kind of device for controlling the discharge of chemical engineering industry exhaust gas includes chemical furnace 1, high-temp waste gas capture smoke pipe 2, high temperature
Middle pressure air-introduced machine 3, high temperature smoke pipe 4 further include reversion type refrigeration condensing tower 5, low temperature snorkel 6, chemical emission absorption and control area
7, waste gas circulation control terminal 8.The capture smoke pipe 2 of the exit setting high-temp waste gas of 1 exhaust gas of work stove, captures the import of smoke pipe 2
It is connect with the waste gas outlet of chemical furnace 1, the air-vent of pressure air-introduced machine connects in the outlet of capture smoke pipe 2 and high temperature；It is pressed in high temperature
The exhaust outlet of air-introduced machine 3 is connect by high temperature smoke pipe 4 with the import smoke pipe of one group of reversion type refrigeration condensing tower 5, one group of reversion type
Refrigeration condensing tower 5 simplifies work high-temp waste gas partial pressure for dropping；Reversion type refrigeration condensing tower 5 passes through low temperature snorkel 6 and chemical industry
Exhaust gas absorption and control area 7 connects, and waste gas circulation control terminal is arranged in the end in chemical emission absorption and control area 7, is used for adjustingization
The internal circulating load of work exhaust gas；In the adjacent setting liquefaction electrolytic furnace 9 of chemical furnace 1, for producing waste residue waste material and recycling dust, liquid
The outlet for changing electrolytic furnace 9 presses the air-vent of air-introduced machine 3 to connect by being electrolysed furnace exhaust capture smoke pipe 10 with high temperature, such as Fig. 1 institutes
Show.
One group of reversion type refrigeration condensing tower 5 in the junction of draught fan system includes the reversion type refrigeration of left, center, right three
Condensing tower 5,5 ontology of each reversion type refrigeration condensing tower is interior to be arranged moisture trap 11, and condensed exhaust gas is supplied gas by low temperature
Pipe 6 is sent to chemical emission absorption and control area 7；The air inlet of the high-temp waste gas at 5 top of reversion type refrigeration condensing tower of arranged on left and right sides
It is connect with high temperature smoke pipe 4, outlet is connect with medium temperature exhaust gas inlet 12, and medium temperature exhaust gas inlet 12 is connected in intermediate reversion type system
The lower part of cold condensing tower 5；The exhaust of the air inlet pipe and left and right reversion type refrigeration condensing tower 5 of intermediate reversion type refrigeration condensing tower 5
Mouth connection, outlet flue are connect with low temperature snorkel 6.As shown in Figure 2.
The low temperature waste gas import 13 in chemical emission absorption and control area 7 is connect with low temperature snorkel 6, chemical emission absorption and control
Setting is multiple successively by the chemical emission absorption and control room 14 of placed in series in the region in area 7, and the absorption backfill of material 15 is in chemical industry
In exhaust gas absorption and control area 7, outside chemical emission absorption and control room 14；Low temperature waste gas import 13 and first chemical emission adsorb
The inlet and outlet of 14 unicom of control room, absorption and control area pass through cross over pipe 16 and waste gas circulation control terminal unicom 8；Waste gas circulation control
The inside setting exhaust gas control terminal adsorption chamber 17 of terminal unicom 8 processed, exhaust gas is by being arranged in waste gas circulation control terminal unicom 8
18 discharge of waste gas circulation outlet of side.As Fig. 3 shows.
Liquefaction electrolytic furnace 9 is located at the top in liquid cooling solid-state pond 23；Setting one is useless above the left side of liquefaction electrolytic furnace 9
An electrolysis taphole 21 is arranged in the feed inlet 19 of slag waste material, one recycling dust feed inlet 20 of right side top setting, lower part,
Top is arranged a high-temp waste gas and exports 22, and high-temp waste gas outlet 22 captures smoke pipe 2 with high-temp waste gas and is connected to.
The method that control chemical engineering industry exhaust gas discharge is carried out using above-mentioned apparatus, specially：The Industry Waste that chemical furnace 1 generates
Gas is captured by high-temp waste gas after smoke pipe 2 captures, and is sent by high temperature smoke pipe 4 after being pressed air-introduced machine 3 to deflect from high temperature adjacent thereto
After in the ontology of reversion type refrigeration condensing tower 5, for high-temp waste gas after refrigeration condenses, the partial pressure of its coefficient of expansion is down to environment
When temperature, then the region for sending smoke pipe 6 to be sent into chemical emission absorption and control area 7 by the low temperature of the condensing tower 5 of intermediate precedence is inhaled
It is attached, and regulated and controled by waste gas circulation control terminal 8, realize chemical engineering industry zero waste gas emission.It is produced when the industrial waste gas that chemical furnace 1 generates
Raw waste residue, waste material and recycling dust is liquefied rapidly under the working condition of liquefaction electrolytic furnace 9, and liquid is in liquefaction electrolytic furnace 9
Liquid outlet 21 water conservancy diversion under influent cooling solid-state pond 23 pond in, stored at solid object after being cooled, eliminate chemical industry
Stove 1 waste residue, waste material caused by production process and the secondary pollution for recycling dust.
Claims (9)
1. a kind of device for controlling the discharge of chemical engineering industry exhaust gas, which is characterized in that the outlet of described chemical furnace (1) exhaust gas
The capture smoke pipe (2) of place's setting high-temp waste gas, the import for capturing smoke pipe (2) are connect with the waste gas outlet of chemical furnace (1), capture cigarette
The air-vent of pressure air-introduced machine connects in the outlet of pipe (2) and high temperature；The exhaust outlet of air-introduced machine (3) is pressed to pass through high temperature smoke pipe in high temperature
(4) it is connect with the import smoke pipe of one group of reversion type refrigeration condensing tower (5)；Reversion type refrigeration condensing tower (5) passes through low temperature snorkel
(6) it is connect with chemical emission absorption and control area (7), the end setting waste gas circulation in chemical emission absorption and control area (7) controls eventually
End, the internal circulating load for adjusting chemical emission；The adjacent setting liquefaction electrolytic furnace (9) of chemical furnace (1), liquefaction electrolytic furnace (9)
Outlet by be electrolysed furnace exhaust capture smoke pipe (10) in high temperature pressure air-introduced machine (3) air-vent connect.
2. a kind of device for controlling the discharge of chemical engineering industry exhaust gas according to claim 1, which is characterized in that described
One group of reversion type refrigeration condensing tower (5) includes the reversion type refrigeration condensing tower (5) of left, center, right three, each reversion type refrigeration condensation
Setting moisture trap (11) in tower (5) ontology, condensed exhaust gas are sent to chemical emission absorption control by low temperature snorkel (6)
Area (7) processed；The air inlet and high temperature smoke pipe of high-temp waste gas at the top of the reversion type refrigeration condensing tower (5) of the arranged on left and right sides
(4) it connects, outlet is connect with medium temperature exhaust gas inlet (12), and the medium temperature exhaust gas inlet (12) is connected in intermediate reversion type
The lower part of refrigeration condensing tower (5)；The air inlet pipe of the reversion type refrigeration condensing tower (5) of the centre is freezed with left and right reversion type
The exhaust outlet of condensing tower (5) connects, and outlet flue is connect with low temperature snorkel (6).
3. a kind of device for controlling the discharge of chemical engineering industry exhaust gas according to claim 1 or 2, which is characterized in that institute
The low temperature waste gas import (13) in the chemical emission absorption and control area (7) stated is connect with low temperature snorkel (6), chemical emission absorption control
It is arranged in the region of area (7) processed multiple successively by the chemical emission absorption and control room (14) of placed in series, absorption material (15) time
It fills in chemical emission absorption and control area (7), chemical emission absorption and control room (14) outside；The low temperature waste gas import (13)
With first chemical emission absorption and control room (14) unicom, the last one chemical emission absorption and control room (14) passes through cross over pipe
(16) with waste gas circulation control terminal unicom (8)；The inside setting exhaust gas of the waste gas circulation control terminal unicom (8) controls
Terminal adsorption chamber (17), exhaust gas is by being arranged waste gas circulation outlet (18) row in waste gas circulation control terminal unicom (8) side
Go out；The peripheral carrier of the waste gas circulation control terminal (8) is built up by the sealing material of non-proliferation.
4. a kind of device for controlling the discharge of chemical engineering industry exhaust gas according to claim 1 or 2, which is characterized in that institute
The liquefaction electrolytic furnace (9) stated is located at the top of liquid cooling solid-state pond (23)；Setting one above the side of liquefaction electrolytic furnace (9)
The feed inlet (19) of waste residue waste material, one recycling dust feed inlet (20) of other side top setting, lower part are arranged an electrolysis and melt
Liquid exports (21), and top is arranged a high-temp waste gas and exports (22), and high-temp waste gas exports (22) and captures smoke pipe (2) with high-temp waste gas
Connection.
5. a kind of device for controlling the discharge of chemical engineering industry exhaust gas according to claim 3, which is characterized in that described
Liquefaction electrolytic furnace (9) is located at the top of liquid cooling solid-state pond (23)；One waste residue is set above the side of liquefaction electrolytic furnace (9)
The feed inlet (19) of waste material, one recycling dust feed inlet (20) of other side top setting, lower part are arranged an electrolysis melt and go out
Mouth (21), top are arranged a high-temp waste gas and export (22), and high-temp waste gas exports (22) and high-temp waste gas capture smoke pipe (2) even
It is logical.
6. a kind of device for controlling the discharge of chemical engineering industry exhaust gas according to claims 1 or 2 or 5, which is characterized in that
The absorption material (15) includes volcanic rock, lime stone, metallurgical industry slag, coal-fired industry slag, mineral hot furnace slag.
7. a kind of device for controlling the discharge of chemical engineering industry exhaust gas according to claim 3, which is characterized in that described
It includes volcanic rock, lime stone, metallurgical industry slag, coal-fired industry slag, mineral hot furnace slag to adsorb material (15).
8. a kind of device for controlling the discharge of chemical engineering industry exhaust gas according to claim 4, which is characterized in that described
It includes volcanic rock, lime stone, metallurgical industry slag, coal-fired industry slag, mineral hot furnace slag to adsorb material (15).
9. the method for carrying out control chemical engineering industry exhaust gas discharge using any devices of claim 1-8, it is characterised in that
Following steps：After the industrial waste gas that the chemical furnace 1 generates captures smoke pipe (2) capture by high-temp waste gas, drawn by pressure in high temperature
After wind turbine (3) is sent into the ontology of reversion type refrigeration condensing tower (5) adjacent thereto after deflecting from by high temperature smoke pipe (4), high temperature is useless
After refrigeration condenses, the partial pressure of its coefficient of expansion reduces gas, when the temperature drop of high-temp waste gas reduces to environment temperature, then in
Between precedence condensing tower (5) low temperature send smoke pipe (6) be sent into chemical emission absorption and control area (7) region adsorbed, and by
Waste gas circulation control terminal (8) regulates and controls, and realizes chemical engineering industry zero waste gas emission；It is generated when the industrial waste gas that chemical furnace (1) generates
Waste residue, waste material and recycling dust liquefaction electrolytic furnace (9) working condition under liquefied rapidly, liquid liquefaction electrolytic furnace
(9) it under the water conservancy diversion of liquid outlet (21) in the pond of influent cooling solid-state pond (23), stores, eliminates at solid object after being cooled
Chemical furnace (1) waste residue, waste material caused by production process and the secondary pollution for recycling dust.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710054135.XA CN108339365B (en) | 2017-01-24 | 2017-01-24 | Device and method for controlling chemical industry waste gas emission |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710054135.XA CN108339365B (en) | 2017-01-24 | 2017-01-24 | Device and method for controlling chemical industry waste gas emission |
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| CN108339365A true CN108339365A (en) | 2018-07-31 |
| CN108339365B CN108339365B (en) | 2020-09-25 |
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| CN103962363A (en) * | 2013-12-27 | 2014-08-06 | 吉天师能源科技(上海)有限公司 | Harmless high-temperature plasma broad-spectrum waste treatment system |
| CN204412010U (en) * | 2014-12-28 | 2015-06-24 | 山东华泰英特罗斯化工有限公司 | Chemical emission treating apparatus |
| CN205146870U (en) * | 2015-11-10 | 2016-04-13 | 吴兆齐 | Cities and towns municipal solid waste processing system with bag collector |
| CN105727681A (en) * | 2016-03-15 | 2016-07-06 | 江苏同庆安全科技有限公司 | Device and processing process for high-boiling-point organic waste gas |
| CN106215691A (en) * | 2016-07-28 | 2016-12-14 | 山东天景工程设计有限公司 | Chemical spent material processing means and process technique |
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