CN206045718U - A kind of flue-gas purification equipment in graphite cathode material carbonization process - Google Patents
A kind of flue-gas purification equipment in graphite cathode material carbonization process Download PDFInfo
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- CN206045718U CN206045718U CN201621046460.9U CN201621046460U CN206045718U CN 206045718 U CN206045718 U CN 206045718U CN 201621046460 U CN201621046460 U CN 201621046460U CN 206045718 U CN206045718 U CN 206045718U
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- condensing tower
- flue
- smoke exhaust
- exhaust pipe
- circulating water
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Abstract
The utility model discloses the flue-gas purification equipment in a kind of graphite cathode material carbonization process, including retort, condensing tower and vacuum receiver, the body of heater side of retort is connected with condensing tower by smoke exhaust pipe；Circulating water intake, circulating water outlet and discharge gate are set on condensing tower, are connected with vacuum receiver by smoke exhaust pipe at the top of condensing tower；Circulating water intake, circulating water outlet and discharge gate are also provided with vacuum receiver, top is connected with water-ring vacuum pump by smoke exhaust pipe.This utility model is capable of achieving high-efficient purification flue gas, reduces work on the spot amount, reduces cost as far as possible.
Description
Technical field
This utility model belongs to filed of flue gas purification, and in particular to the flue gas in a kind of graphite cathode material carbonization process is net
Change processing meanss.
Background technology
In graphite cathode material carbonization process, substantial amounts of tar and steam dissipation are inevitably had, if let alone
Discharge, then can bring serious environmental pollution and the wasting of resources.It is electric fishing and burning using more tar removing method at present, but
It is both approaches equipment complexity, operating cost height.
The content of the invention
In view of deficiency of the prior art, the purpose of this utility model is to provide a kind of graphite cathode material carbonization process
In flue-gas purification equipment, to realize high-efficient purification flue gas, as far as possible reduce work on the spot amount, reduces cost.
To achieve these goals, the technical solution of the utility model is：In a kind of graphite cathode material carbonization process
Flue-gas purification equipment, including retort, the first condensing tower, the second condensing tower and vacuum receiver, the stove of the retort
Connect retort air pressure lid above body, side is connected with the first condensing tower by the first smoke exhaust pipe, while body of heater side arranges true
Reciprocal of duty cycle instrument；First circulation water inlet, first circulation water out and the first discharge gate are set on first condensing tower, and top leads to
Cross the second smoke exhaust pipe to be connected with the second condensing tower；Arrange second circulation water inlet, second circulation water to go out on second condensing tower
Mouth and the second discharge gate, top is connected with vacuum receiver by the 3rd smoke exhaust pipe；Arrange the 3rd to follow on the vacuum receiver
Ring water inlet, the 3rd circulating water outlet and the 3rd discharge gate, top are connected with water-ring vacuum pump by the 4th smoke exhaust pipe；It is described
4th circulating water intake and drain pipe are set on water-ring vacuum pump, filter is set before the 4th circulating water intake.
Further, arrange in first condensing tower multiple vertical placements, parallel, top is connected with bottom
Flue, wherein flue bottom are connected with smoke exhaust pipe import, and flue bottom is also connected with the first discharge gate,
Also it is connected with the first smoke exhaust pipe at the top of flue, is condensing tower inner chamber outside flue, with first circulation water inlet and the
One circulating water outlet is connected；Second condensing tower and the first condensing tower internal structure are identical.
Smoke exhaust pipe and vacuum instrument are retrofitted in retort side by this utility model, can so make execute-in-place simple,
Smoke exhaust pipe is hardly damaged, and vacuum instrument is difficult to be plugged, and reduces work on the spot amount；Smoke exhaust pipe adopts tube material, cost
It is low and durable, it is easy to clean；Connected by two condensing towers, the tar in flue gas by repeats condensation, under gravity successively from
Condensing tower discharge gate is discharged, and can so cause the tar in flue gas to be substantially efficiently recycled utilizations, is reduced to environment dirt
Dye.
Description of the drawings
Fig. 1 is this utility model structural representation.
In figure：1- retorts, 2- retort air pressure lids, 3- vacuum instrument, the first smoke exhaust pipes of 4-, the first condensing towers of 5-,
6- first circulation water inlets, the first discharge gates of 7-, 8- first circulation water outs, the second smoke exhaust pipes of 9-, the second condensing towers of 10-, 11-
Second circulation water inlet, the second discharge gates of 12-, 13- second circulation water outs, the 3rd smoke exhaust pipes of 14-, 15- vacuum receivers,
The 3rd circulating water intakes of 16-, the 3rd discharge gates of 17-, the 3rd circulating water outlets of 18-, the 4th smoke exhaust pipes of 19-, 20- liquid-ring type vacuum
Pump, the 4th circulating water intakes of 22-, 21- drain pipies, 23- filters.
Fig. 2 is this utility model the first condensing tower internal structure schematic diagram.
In figure：The first condensing towers of 5-, 5-1- the first condensing tower inner chambers, 5-2- the first condensing tower flues.
Specific embodiment
With reference to the accompanying drawings and examples this utility model is described further.
Referring to Fig. 1, the flue-gas purification equipment in a kind of graphite cathode material carbonization process, including retort 1, first
Condensing tower 5, the second condensing tower 10 and vacuum receiver 15, connect retort air pressure lid 2, side above the body of heater of the retort
It is connected with the first condensing tower by the first smoke exhaust pipe 4, while body of heater side arranges vacuum instrument 3；On first condensing tower
First circulation water inlet 6, first circulation water out 8 and the first discharge gate 7 are set, and top is cold with second by the second smoke exhaust pipe 9
Solidifying tower connection；Second circulation water inlet 11, second circulation water out 13 and the second discharge gate 12 are set on second condensing tower,
Top is connected with vacuum receiver by the 3rd smoke exhaust pipe 14；Arrange on the vacuum receiver the 3rd circulating water intake 16, the
Three circulating water outlets 18 and the 3rd discharge gate 17, top are connected with water-ring vacuum pump 20 by the 4th smoke exhaust pipe 19；The water
4th circulating water intake 22 and drain pipe 21 are set on ring vacuum pumps.Filter 23 is set before the 4th circulating water intake.
Multiple vertical placements, parallel, the flue 5- that top is connected with bottom are respectively provided with first condensing tower 5
2, wherein flue bottom is connected with smoke exhaust pipe import 4, and flue bottom is also connected with the first discharge gate 7, flue gas
Also it is connected with the first smoke exhaust pipe 9 at the top of pipeline；It is condensing tower inner chamber 5-1 outside flue, with first circulation water inlet 6 and the
One circulating water outlet 8 is connected.Condensing tower 10 is identical with 5 internal structure of condensing tower.
The flue gas produced after carbonization（500-600℃）From retort 1 out, condensing tower 5 is entered into by smoke exhaust pipe 4, when
When recirculated water is opened, condensing tower inner chamber 5-1 can be full of circulating condensing water, and flue gas is from the first smoke exhaust pipe 4 into the first condensation tower flue gas
Pipeline 5-2, is discharged from discharge gate 7 after now the most of tar in flue gas is condensed under gravity；Flue gas continues from cold
Solidifying tower 5 out, enters into condensing tower 10 by smoke exhaust pipe 9, and condensing tower 10 is identical with 5 internal structure of condensing tower, now in flue gas
Fraction tar it is condensed again after discharge from discharge gate 12 under gravity；Flue gas from condensing tower 10 out, by row
Smoke pipe 14 enters into vacuum receiver 15, under gravity from row after now the remainder tar in flue gas is condensed again
Material mouth 17 is discharged again；Flue gas from vacuum receiver 15 out, because of 20 vacuum action of water-ring vacuum pump under, by smoke exhaust pipe
19 enter into water-ring vacuum pump 20 simultaneously with recirculated water 22, last remaining cigarette and water from water-ring vacuum pump 20 out, by row
Water pipe 21 is discharged.
The foregoing is only better embodiment of the present utility model, all impartial changes done according to this utility model with repair
Decorations, should all belong to covering scope of the present utility model.
Claims (2)
1. a kind of flue-gas purification equipment in graphite cathode material carbonization process, including retort, the first condensing tower, second
Condensing tower and vacuum receiver, above the body of heater of the retort connect retort air pressure lid, side by the first smoke exhaust pipe with
First condensing tower connects, while body of heater side arranges vacuum instrument；On first condensing tower arrange first circulation water inlet,
First circulation water out and the first discharge gate, top are connected with the second condensing tower by the second smoke exhaust pipe；Second condensing tower
Upper setting second circulation water inlet, second circulation water out and the second discharge gate, top is by the 3rd smoke exhaust pipe and vacuum reservoir
Tank connects；3rd circulating water intake, the 3rd circulating water outlet and the 3rd discharge gate are set on the vacuum receiver, and top passes through
4th smoke exhaust pipe is connected with water-ring vacuum pump；4th circulating water intake and drain pipe, institute are set on the water-ring vacuum pump
Before stating the 4th circulating water intake, filter is set.
2. flue-gas purification equipment according to claim 1, it is characterised in that arrange in first condensing tower multiple
Vertically placing, the parallel, flue that top is connected with bottom, wherein flue bottom is connected with smoke exhaust pipe import
Logical, flue bottom is also connected with the first discharge gate, is also connected with the first smoke exhaust pipe at the top of flue；Flue
It is condensing tower inner chamber outward, is connected with first circulation water inlet and first circulation water out；Second condensing tower and the first condensing tower
Internal structure is identical.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621046460.9U CN206045718U (en) | 2016-09-10 | 2016-09-10 | A kind of flue-gas purification equipment in graphite cathode material carbonization process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621046460.9U CN206045718U (en) | 2016-09-10 | 2016-09-10 | A kind of flue-gas purification equipment in graphite cathode material carbonization process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206045718U true CN206045718U (en) | 2017-03-29 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621046460.9U Active CN206045718U (en) | 2016-09-10 | 2016-09-10 | A kind of flue-gas purification equipment in graphite cathode material carbonization process |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108007248A (en) * | 2017-12-29 | 2018-05-08 | 江苏省特种设备安全监督检验研究院南通分院 | A kind of gas fired-boiler graphite condenser and preparation method thereof |
| CN109004193A (en) * | 2018-07-18 | 2018-12-14 | 大同新成新材料股份有限公司 | A kind of negative electrode of lithium ion battery carbonizing plant and its carbonization method |
-
2016
- 2016-09-10 CN CN201621046460.9U patent/CN206045718U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108007248A (en) * | 2017-12-29 | 2018-05-08 | 江苏省特种设备安全监督检验研究院南通分院 | A kind of gas fired-boiler graphite condenser and preparation method thereof |
| CN108007248B (en) * | 2017-12-29 | 2023-12-19 | 江苏省特种设备安全监督检验研究院南通分院 | Graphite condenser for gas boiler and preparation method thereof |
| CN109004193A (en) * | 2018-07-18 | 2018-12-14 | 大同新成新材料股份有限公司 | A kind of negative electrode of lithium ion battery carbonizing plant and its carbonization method |
| CN109004193B (en) * | 2018-07-18 | 2020-07-28 | 大同新成新材料股份有限公司 | Lithium ion battery cathode carbonization device and carbonization method thereof |
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