CN109173597A - A kind of storage battery production processing waste gas recovery processing unit - Google Patents
A kind of storage battery production processing waste gas recovery processing unit Download PDFInfo
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- CN109173597A CN109173597A CN201811090420.8A CN201811090420A CN109173597A CN 109173597 A CN109173597 A CN 109173597A CN 201811090420 A CN201811090420 A CN 201811090420A CN 109173597 A CN109173597 A CN 109173597A
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- spray chamber
- chamber
- pipe
- waste gas
- storage battery
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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
- 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
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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
- 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
- B01D53/1418—Recovery of products
-
- 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
- B01D53/1493—Selection of liquid materials for use as absorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2252/00—Absorbents, i.e. solvents and liquid materials for gas absorption
- B01D2252/10—Inorganic absorbents
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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)
- Treating Waste Gases (AREA)
Abstract
The present invention relates to technical field of waste gas treatment, and it is an object of the present invention to provide a kind of storage battery production processing waste gas recovery processing unit that resource reclaim may be implemented.Used technical solution is: a kind of storage battery production processing waste gas recovery processing unit, the tower body including being successively separated into upper spray chamber, lower spray chamber and crystallisation chamber from top to bottom；Air inlet pipe is arranged in the lower spray chamber lower part, and the tower body side wall setting is connected to the gas pipeline on lower spray chamber top and upper spray chamber lower part, exhaust outlet is arranged at the top of the upper spray chamber；The upper spray pipe network of setting and lower spray pipe network are respectively corresponded in the upper spray chamber and lower spray chamber, the upper spray chamber bottom setting is connected to the outlet pipe of lower spray pipe network；Setting charge pipe is connected to by filtrate return pipe with upper spray pipe network with the inlet, bottom setting discharge port and filtrate (liquid, the filtrate (liquid that are connected to down spray chamber bottom at the top of the crystallisation chamber.The present invention can be recycled the ammonia in exhaust gas.
Description
Technical field
The present invention relates to technical field of waste gas treatment, and in particular to a kind of storage battery production processing waste gas recovery processing dress
It sets.
Background technique
Battery can generate a large amount of ammonia-contaminated gas in the process of production and processing, and the prior art is usually to be passed directly into exhaust gas
It is absorbed in absorption tower, cannot achieve the recycling to ammonia.Therefore, it is necessary to study one kind, and resource reclaim may be implemented
Storage battery production processing use waste gas recovery processing unit.
Summary of the invention
The purpose of the present invention is to provide at a kind of storage battery production processing waste gas recovery that resource reclaim may be implemented
Manage device.
To achieve the above object, the technical solution adopted by the present invention is that:
A kind of storage battery production processing waste gas recovery processing unit, including tower body, the tower body successively divide from top to bottom
It is divided into spray chamber, lower spray chamber and crystallisation chamber；Air inlet pipe, the tower body side wall setting connection is arranged in the lower spray chamber lower part
Exhaust outlet is arranged in the gas pipeline on lower spray chamber top and upper spray chamber lower part, the upper spray chamber top；The upper spray chamber
It upper spray pipe network and lower spray pipe network is set and is adapted to spray head with being respectively corresponded in lower spray chamber, the upper spray chamber bottom
The outlet pipe for being connected to lower spray pipe network is set；The feed liquor that charge pipe is set at the top of the crystallisation chamber and is connected to down spray chamber bottom
Mouth, bottom setting discharge port and filtrate (liquid, the filtrate (liquid are connected to by filtrate return pipe with upper spray pipe network.
Preferably, last time water pipe is arranged in the upper spray chamber lower part, and the last time water pipe is connected to upper spray pipe network；It is described
Water pipe, the water pipe next time are connected to the setting of lower spray chamber lower part with lower spray pipe network next time.
Preferably, PH sensor, the PH are provided in the upper spray chamber bottom, lower spray chamber bottom and crystallisation chamber
Sensor is electrically connected with the controller.
Preferably, the last time water pipe, water pipe, filtrate return pipe, outlet pipe and inlet are respectively set by controlling next time
The solenoid valve of device control.
Preferably, muti-piece diaphragm plate is respectively set side by side along the vertical direction in the upper spray chamber and lower spray chamber, it is described
Muti-piece diaphragm plate is staggered gas-liquid channel in left and right ends；The upper spray pipe network is evenly distributed on the indoor tabula of spray
Below plate, the lower spray pipe network is evenly distributed below the lower indoor diaphragm plate of spray.
Preferably, the crystallisation chamber is made of the collecting chamber of the crystallization cavity on top and lower part, and the inlet goes out with filtrate
Mouth is located at the left and right ends of crystallization cavity, and the charge pipe is corresponding with the position of inlet；It is set side by side in the crystallization cavity
More or so run through the condenser pipe of crystallization cavity；Muti-piece vertical clapboard, the muti-piece is set side by side in the crystallization cavity in left-right direction
Vertical clapboard is staggered filtrate channel in upper and lower ends, and strainer is arranged in the filtrate channel；The crystallization cavity bottom setting is multiple
Crystallization outlet, the crystallization outlet are distributed between vertical clapboard and vertical clapboard, vertical clapboard and crystallization cavity wall, the crystallization outlet
The solenoid valve controlled by controller is set.
Preferably, the collecting chamber is funnel-shaped, and the center of collecting chamber bottom is arranged in the discharge port.
Preferably, agitating device is set in the crystallization cavity, and the agitating device is located at charge pipe and crystallization cavity interconnecting part
The lower section of position.
Preferably, the top of the upper spray chamber is in a circular table shape and activated carbon adsorption layer is arranged.
Preferably, gas dispersion apparatus is arranged in the lower spray chamber lower part, and the gas dispersion apparatus includes along level side
Shaft to extension and the blade that is arranged in shaft, the side wall that the shaft passes through lower spray chamber are connect with servo motor.
Beneficial effects of the present invention embody a concentrated reflection of, the present invention tower body is successively separated into from top to bottom upper spray chamber, under
Spray chamber and crystallisation chamber；Exhaust gas is poured into lower spray column lower part by air inlet pipe；Exhaust gas can flow up, and pass through gas pipeline
Enter upper spray chamber lower part from lower spray chamber top, finally from the exhaust outlet discharge at the top of upper spray chamber.Upper spray chamber and lower spray
Leaching interior is respectively arranged with spray pipe network and lower spray pipe network, and upper spray pipe network and lower spray pipe network can be sprayed by spray head
Phosphoric acid solution purifies exhaust gas and generates ammonium dihydrogen phosphate.Phosphorus acid content is higher in solution in upper spray chamber, di(2-ethylhexyl)phosphate
Hydrogen ammonium content is lower, the ammonia in exhaust gas can be fully absorbed；Phosphorus acid content is lower in solution in lower spray column, di(2-ethylhexyl)phosphate
Hydrogen ammonium content is higher, and the temperature for the exhaust gas being just passed through is higher, can make to dissolve as far as possible in the lower indoor solution of spray in this way
More ammonium dihydrogen phosphates；Solution in upper spray chamber can enter lower spray pipe network by outlet pipe and be sprayed onto lower spray chamber
In, the solution in lower spray chamber can be discharged into crystallisation chamber by the inlet at the top of crystallisation chamber；By feed inlet to crystallisation chamber
Interior addition phosphoric acid adjusts pH value, and is cooled down to solution, the biphosphate crystalline ammonium in solution is precipitated, that is, can be recycled
To ammonium dihydrogen phosphate crystal；At this point, the phosphorus acid content of solution increases in crystallisation chamber, determining ammonium biphosphate content reduces, and can lead to
Filtered fluid return pipe is pumped into upper spray chamber and recycles.The present invention is not only realized to be generated in storage battery production process
Ammonia-contaminated gas purification, also ammonia is recycled；It is real and by the way that upper spray column, lower spray column, crystallizing tower is arranged
Show the gradient type absorption to ammonia-contaminated gas, not only makes the purification to exhaust gas more thorough, but also phosphoric acid solution is allowed to have obtained more
Adequately utilize.
Detailed description of the invention
Fig. 1 is structural schematic diagram of the invention；
Fig. 2 is the structural schematic diagram of upper spray chamber；
Fig. 3 is the structural schematic diagram of lower spray chamber；
Fig. 4 is the structural schematic diagram of crystallisation chamber.
Specific embodiment
1~4 the present invention is further explained with reference to the accompanying drawing.
A kind of storage battery production processing waste gas recovery processing unit, including tower body, the tower body successively divide from top to bottom
It is divided into spray chamber 1, lower spray chamber 2 and crystallisation chamber 3.Air inlet pipe 4 is arranged in 2 lower part of lower spray chamber, and the tower body side wall is set
The gas pipeline 5 for being connected to lower 1 lower part of 2 top of spray chamber and upper spray chamber is set, exhaust outlet 6 is set at the top of the upper spray chamber 1.Institute
It states and respectively corresponds the upper spray pipe network 7 of setting and lower spray pipe network 8 in spray chamber 1 and lower spray chamber 2 and be adapted to spray head 9, institute
State the outlet pipe 10 that the setting of 1 bottom of spray chamber is connected to lower spray pipe network 8.Charge pipe 11 is set at the top of the crystallisation chamber 3 and is connected
Inlet 12, bottom setting discharge port 13 and the filtrate (liquid of logical lower 2 bottom of spray chamber, it should be appreciated that the charge pipe
11 for adding phosphoric acid into crystallisation chamber 3.The filtrate (liquid is connected to by filtrate return pipe 14 with upper spray pipe network 7.It should
Understand, filtrate return pipe 14 is provided with the water pump to draw water upwards.
Further, last time water pipe 15, the last time water pipe 15 and upper spray pipe network 7 is arranged in 1 lower part of upper spray chamber
Connection；Water pipe 16, the water pipe next time 16 are connected to lower spray pipe network 8 next time for 2 lower part of the lower spray chamber setting.It should be understood that
, the last time water pipe 15 and next time water pipe 16 be provided with the water pump to draw water upwards, and last time water pipe 15 can be by upper spray
The solution of 1 bottom of room is pumped into spray pipe network 7 again and is sprayed, and water pipe 16 can be by the solution of lower 2 bottom of spray chamber next time
Again lower spray pipe network 8 is pumped into be sprayed.
Further, it is provided with PH sensor in 1 bottom of upper spray chamber, 2 bottom of lower spray chamber and crystallisation chamber 3,
The PH sensor is electrically connected with the controller.It should be understood that can judge upper spray chamber 1, lower spray by detection pH value
Drench the phosphorus acid content and ammonium dihydrogen phosphate saturation degree in the solution in room 2 and crystallisation chamber 3.
Further, the last time water pipe 15, water pipe 16, filtrate return pipe 14, outlet pipe 10 and inlet 12 divide next time
The solenoid valve that She Zhi not be controlled by controller.It should be understood that when the solution in upper spray chamber 1, lower spray chamber 2, crystallisation chamber 3
When reaching preset pH value, controller can open corresponding solenoid valve, in upper spray chamber 1, lower spray chamber 2 or crystallisation chamber 3
Spray liquid carries out extraction, compared with common valve, by the solenoid valve of controller control without manually being operated, and intelligence degree
Height, stability are good.
Embodiments of the present invention are described below, exhaust gas is poured by lower spray column lower part by air inlet pipe 4；Exhaust gas can be upward
Flowing, and enter upper 1 lower part of spray chamber from lower 2 top of spray chamber by gas pipeline 5, and finally from upper 1 top of spray chamber
Exhaust outlet 6 is discharged；Spray pipe network 7 and lower spray pipe network 8, upper spray tube are respectively arranged in upper spray chamber 1 and lower spray chamber 2
Net 7 and lower spray pipe network 8 can be sprayed phosphoric acid solution by spray head 9 and be purified to exhaust gas and generate ammonium dihydrogen phosphate.Upper spray
It drenches in the solution in room 1 that phosphorus acid content is higher, determining ammonium biphosphate content is lower, the ammonia in exhaust gas can be fully absorbed；With
Solution in upper spray chamber 1 constantly absorb ammonia, the pH value of solution will increase, when to pH value increase to a certain extent, control
Device can open the solenoid valve of outlet pipe 10 and filtrate return pipe 14, and the solution in upper spray chamber 1 is discharged into lower spray chamber 2, and
Filtrate in crystallisation chamber 3 is pumped into upper spray chamber 1.The phosphorus acid content of solution is lower in lower spray chamber 2, determining ammonium biphosphate content
It is higher, and the temperature of exhaust gas is higher, can make ammonium dihydrogen phosphate as much as possible in the solution in lower spray chamber 2 in this way, when molten
When the saturation degree of ammonium dihydrogen phosphate reaches preset value in liquid, controller can open the inlet 12 at the top of crystallisation chamber 3, by lower spray
Solution in room 2 is discharged into crystallisation chamber 3.Phosphoric acid is added into crystallisation chamber 3 by feed inlet, adjusts pH value, and will be in solution
Biphosphate crystalline ammonium is precipitated, i.e., recyclable to obtain ammonium dihydrogen phosphate crystal；At this point, in crystallisation chamber 3 solution phosphorus acid content liter
High, determining ammonium biphosphate content reduces, and can be pumped into upper spray chamber 1 and be recycled by filtrate return pipe 14.The present invention is not
The purification to the ammonia-contaminated gas generated in storage battery production process is only realized, also ammonia is recycled；And
By the way that upper spray column, lower spray column, crystallizing tower is arranged, the gradient type absorption to ammonia-contaminated gas is realized, is not only made to exhaust gas
Purification it is more thorough, and phosphoric acid solution is allowed to have obtained more fully utilizing.
It advanced optimizes as of the invention, is respectively set side by side along the vertical direction in the upper spray chamber 1 and lower spray chamber 2
Set muti-piece diaphragm plate 19, the muti-piece diaphragm plate 19 is staggered gas-liquid channel in left and right ends；The upper spray pipe network 7 is uniformly
It is distributed in 19 lower section of diaphragm plate in spray chamber 1, the lower spray pipe network 8 is evenly distributed on the diaphragm plate in lower spray chamber 2
19 lower sections.It should be understood that upper spray chamber 1 and lower spray chamber 2 are separated into multilayer by diaphragm plate 19, exhaust gas can only be along adjacent cross
Gap and gas-liquid channel between partition 19 or so, which are wriggled, to be flowed up, so, interior in a limited space, is greatly increased
The length of exhaust gas travel path, enables exhaust gas more fully to be reacted with spray liquid, has saved space occupied, improves
Clean-up effect.
Further, the crystallisation chamber 3 is made of the collecting chamber 21 of the crystallization cavity 20 on top and lower part, the inlet 12
The left and right ends of crystallization cavity 20 are located at filtrate (liquid, the charge pipe 11 is corresponding with the position of inlet 12；The knot
More or so the condenser pipes 22 for running through crystallization cavity 20 are set side by side in brilliant chamber 20；It is set side by side in left-right direction in the crystallization cavity 20
Set muti-piece vertical clapboard 23, the muti-piece vertical clapboard 23 is staggered filtrate channel in upper and lower ends, the filtrate channel setting filter
Net 24；Multiple crystallization outlets 25 are arranged in 20 bottom of crystallization cavity, and the crystallization outlet 25 is distributed in vertical clapboard 23 and vertical clapboard
23, between 20 inner wall of vertical clapboard 23 and crystallization cavity, the solenoid valve controlled by controller is arranged in the crystallization outlet 25.It should be understood that
, phosphoric acid can be added into crystallization cavity 20 by charge pipe 11 to adjust the PH of solution in crystallization cavity 20, and pass through condensation
Pipe 22 cools down to the solution in crystallization cavity 20, and the biphosphate crystalline ammonium in solution is precipitated；At regular intervals, it controls
Device will open the solenoid valve of primary crystallization outlet 25, sink to the crystallization of 20 bottom of crystallization cavity in collecting chamber 21；Work as collecting chamber
After collecting full crystallization in 21, the solution in collecting chamber 21 can be squeezed into crystallization cavity 20, close the solenoid valve, simultaneously of crystallization outlet 25
The solenoid valve for opening discharge port 13, the crystallization in collecting chamber 21 can be discharged.In addition, crystallization cavity 20 is separated by vertical clapboard 23
Multiple Vertical Channels, inlet 12 and filtrate (liquid are located at the left and right ends of crystallization cavity 20；When solution from inlet 12 to
When filtrate (liquid is advanced, it can make to carry out gradient type condensation to solution, the ammonium dihydrogen phosphate in solution is made gradually to crystallize precipitation simultaneously
It is deposited on 20 bottom of crystallization cavity, so, the determining ammonium biphosphate content in filtrate (liquid, solution is lower
Easily realize the separation of crystal and solution.
Further, the collecting chamber 21 is funnel-shaped, and the center of 21 bottom of collecting chamber is arranged in the discharge port 13.It answers
It when understanding, can be configured by controller, open the solenoid valve of a discharge port 13 at regular intervals, will collect
Crystal discharge in chamber 21；Crystal can be made to converge to discharge port 13 the setting funnel of collecting chamber 21, convenient for the row of crystal
Out and collect.
Further, agitating device is set in the crystallization cavity 20, the agitating device is located at charge pipe 11 and crystallization cavity
The lower section at 20 connection positions.It should be understood that agitating device can be such that the phosphoric acid being added in crystallization cavity 20 quickly dissolves.
Further, the top of the upper spray chamber 1 is in a circular table shape and activated carbon adsorption layer 26 is arranged.It should be understood that
It is to be arranged to the top of upper spray chamber 1 round table-like, carries out convergence convenient for purified gas and from 1 top of upper spray chamber
Exhaust outlet 6 is discharged；Activated carbon adsorption layer 26 is set at the top of upper spray chamber 1, spray liquid purified gas can be carried out
It purifies again, pernicious gas is avoided to remain, further increase clean-up effect.
Further, gas dispersion apparatus is arranged in 2 lower part of lower spray chamber, and the gas dispersion apparatus includes along level
The shaft 27 and the blade 18 being arranged in shaft 27 that direction extends, the shaft 27 pass through the side wall and servo of lower spray chamber 2
Motor 17 connects.It should be understood that gas dispersion apparatus the exhaust gas into lower spray chamber 2 can be made quickly and evenly to spread,
It avoids exhaust gas from depositing in a certain position, so that spray liquid be made more fully to react with exhaust gas, improves clean-up effect.
Although specific embodiments of the present invention have been described above, it will be appreciated by those of skill in the art that not
Under the premise of the principle and substance of the present invention, many changes and modifications may be made, but these become
More protection scope of the present invention is each fallen with modification.
Claims (10)
1. a kind of storage battery production processing waste gas recovery processing unit, it is characterised in that: including tower body, the tower body is from upper past
Under be successively separated into spray chamber (1), lower spray chamber (2) and crystallisation chamber (3)；Air inlet pipe is arranged in lower spray chamber (2) lower part
(4), tower body side wall setting is connected to the gas pipeline (5) on lower spray chamber (2) top and upper spray chamber (1) lower part, it is described on
Exhaust outlet (6) are set at the top of spray chamber (1)；The upper spray tube of setting is respectively corresponded in the upper spray chamber (1) and lower spray chamber (2)
Net (7) and lower spray pipe network (8) are simultaneously adapted to spray head (9), and upper spray chamber (1) the bottom setting is connected to lower spray pipe network (8)
Outlet pipe (10)；The inlet that charge pipe (11) are set at the top of the crystallisation chamber (3) and are connected to down spray chamber (2) bottom
(12), bottom setting discharge port (13) and filtrate (liquid, the filtrate (liquid pass through filtrate return pipe (14) and upper spray pipe network
(7) it is connected to.
2. a kind of storage battery production processing waste gas recovery processing unit according to claim 1, it is characterised in that: described
Last time water pipe (15) are arranged in upper spray chamber (1) lower part, and the last time water pipe (15) is connected to upper spray pipe network (7)；The lower spray
Drenching the setting of room (2) lower part, water pipe (16), the water pipe next time (16) are connected to lower spray pipe network (8) next time.
3. a kind of storage battery production processing waste gas recovery processing unit according to claim 2, it is characterised in that: described
PH sensor, the PH sensor and control are provided in upper spray chamber (1) bottom, lower spray chamber (2) bottom and crystallisation chamber (3)
Device electrical connection processed.
4. a kind of storage battery production processing waste gas recovery processing unit according to claim 3, it is characterised in that: described
Last time water pipe (15), next time water pipe (16), filtrate return pipe (14), outlet pipe (10) and inlet (12) are respectively set by controlling
The solenoid valve of device control.
5. according to claim 1 to a kind of storage battery production processing waste gas recovery processing unit described in any one of 4,
It is characterized in that: muti-piece diaphragm plate (19) being respectively set side by side along the vertical direction in the upper spray chamber (1) and lower spray chamber (2),
The muti-piece diaphragm plate (19) is staggered gas-liquid channel in left and right ends；The upper spray pipe network (7) is evenly distributed on spray
It drenches below the diaphragm plate (19) in room (1), the lower spray pipe network (8) is evenly distributed on the diaphragm plate in lower spray chamber (2)
(19) lower section.
6. a kind of storage battery production processing waste gas recovery processing unit according to claim 5, it is characterised in that: described
Crystallisation chamber (3) is made of the collecting chamber (21) of the crystallization cavity (20) on top and lower part, the inlet (12) and filtrate (liquid point
Not Wei Yu crystallization cavity (20) left and right ends, the charge pipe (11) is corresponding with the position of inlet (12)；The crystallization cavity
(20) more or so the condenser pipes (22) for running through crystallization cavity (20) are set side by side in；In the crystallization cavity (20) in left-right direction simultaneously
Column setting muti-piece vertical clapboard (23), the muti-piece vertical clapboard (23) are staggered filtrate channel in upper and lower ends, and the filtrate is logical
Strainer (24) are arranged in road；Multiple crystallization outlets (25) are arranged in crystallization cavity (20) bottom, and the crystallization outlet (25) is distributed in
Between vertical clapboard (23) and vertical clapboard (23), vertical clapboard (23) and crystallization cavity (20) inner wall, crystallization outlet (25) setting by
The solenoid valve of controller control.
7. a kind of storage battery production processing waste gas recovery processing unit according to claim 6, it is characterised in that: described
Collecting chamber (21) is funnel-shaped, center of discharge port (13) setting in collecting chamber (21) bottom.
8. a kind of storage battery production processing waste gas recovery processing unit according to claim 6, it is characterised in that: described
Agitating device is set in crystallization cavity (20), and the agitating device is located at charge pipe (11) and is connected under position with crystallization cavity (20)
Side.
9. a kind of storage battery production processing waste gas recovery processing unit according to claim 1, it is characterised in that: described
The top of upper spray chamber (1) is in a circular table shape and activated carbon adsorption layer (26) are arranged.
10. a kind of storage battery production processing waste gas recovery processing unit according to claim 1, it is characterised in that: institute
Lower spray chamber (2) lower part setting gas dispersion apparatus is stated, the gas dispersion apparatus includes horizontally extending shaft
(27) and blade (18) on shaft (27) is set, the shaft (27) passes through the side wall and servo motor of lower spray chamber (2)
(17) it connects.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811090420.8A CN109173597A (en) | 2018-09-18 | 2018-09-18 | A kind of storage battery production processing waste gas recovery processing unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811090420.8A CN109173597A (en) | 2018-09-18 | 2018-09-18 | A kind of storage battery production processing waste gas recovery processing unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109173597A true CN109173597A (en) | 2019-01-11 |
Family
ID=64908516
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811090420.8A Pending CN109173597A (en) | 2018-09-18 | 2018-09-18 | A kind of storage battery production processing waste gas recovery processing unit |
Country Status (1)
| Country | Link |
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| CN (1) | CN109173597A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2166128A1 (en) * | 1971-12-29 | 1973-08-10 | Olin Corp | |
| CN1049754A (en) * | 1989-08-19 | 1991-03-06 | 重庆蓄电池联合公司 | In neutral medium, revert back the plumbous method of receiving in the scrap battery with electrolysis |
| CN104353337A (en) * | 2014-10-09 | 2015-02-18 | 宜兴市凯特净化设备有限公司 | Recovery processing system and processing method for ammonia-containing waste gas |
| CN205773385U (en) * | 2016-05-19 | 2016-12-07 | 安徽东至广信农化有限公司 | A kind of production equipment for ammonium sulfate |
-
2018
- 2018-09-18 CN CN201811090420.8A patent/CN109173597A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2166128A1 (en) * | 1971-12-29 | 1973-08-10 | Olin Corp | |
| CN1049754A (en) * | 1989-08-19 | 1991-03-06 | 重庆蓄电池联合公司 | In neutral medium, revert back the plumbous method of receiving in the scrap battery with electrolysis |
| CN104353337A (en) * | 2014-10-09 | 2015-02-18 | 宜兴市凯特净化设备有限公司 | Recovery processing system and processing method for ammonia-containing waste gas |
| CN205773385U (en) * | 2016-05-19 | 2016-12-07 | 安徽东至广信农化有限公司 | A kind of production equipment for ammonium sulfate |
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| CB02 | Change of applicant information | ||
| CB02 | Change of applicant information |
Address after: 616850 Haitang Battery Industrial Park, Ganluo County, Liangshan Yi Autonomous Prefecture, Sichuan Province Applicant after: Sichuan Ols New Energy Technology Co., Ltd. Address before: 616850 Haitang Battery Industrial Park, Ganluo County, Liangshan Yi Autonomous Prefecture, Sichuan Province Applicant before: Sichuan Hezhong People's Livelihood New Energy Technology Co., Ltd. |
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| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20190111 |