CN202410640U - Exhaust system for nickel particle dissolving reactor - Google Patents

Exhaust system for nickel particle dissolving reactor Download PDF

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Publication number
CN202410640U
CN202410640U CN2012200224973U CN201220022497U CN202410640U CN 202410640 U CN202410640 U CN 202410640U CN 2012200224973 U CN2012200224973 U CN 2012200224973U CN 201220022497 U CN201220022497 U CN 201220022497U CN 202410640 U CN202410640 U CN 202410640U
Authority
CN
China
Prior art keywords
pipeline
reactor
washing
scrubbing tower
gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2012200224973U
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Chinese (zh)
Inventor
姜纯
柳永乾
陈士军
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JINKE NON-FERROUS METALS CO LTD
Original Assignee
JINKE NON-FERROUS METALS CO LTD
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by JINKE NON-FERROUS METALS CO LTD filed Critical JINKE NON-FERROUS METALS CO LTD
Priority to CN2012200224973U priority Critical patent/CN202410640U/en
Application granted granted Critical
Publication of CN202410640U publication Critical patent/CN202410640U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Treating Waste Gases (AREA)

Abstract

The utility model relates to an exhaust system for a nickel particle dissolving reactor. The system comprises a washing tower, wherein the top of the washing tower is connected with a venturi tube through a pipeline, and the bottom of the washing tower is connected with a washing circulation groove through a pipeline; a pall ring is filled in the washing tower; a drip washing sprayer is arranged in the washing tower; the washing circulation groove is connected with the left side of a washing circulation pump through a pipeline; the right side of the washing circulation pump is connected with the drip washing sprayer through a pipeline; the washing circulation groove is provided with a second exhaust port and is connected with the venturi tube through a pipeline; the washing tower is connected with a graphite condenser through a pipeline; a reactor is arranged beside the graphite condenser; the top of the reactor is provided with a first exhaust port, is connected with the bottom of the graphite condenser through a pipeline, is provided with an emergency exhaust port and is connected with an emergency water seal tank through a pipeline; and the reactor is provided with a backflow port and is connected with the graphite condenser through a pipeline, so that usable gas in tail gas can be recycled, and waste gas can be safely exhausted into the atmosphere.

Description

Nickel shot dissolution reactor gas extraction system
Technical field
The utility model relates to a kind of nickel shot dissolution reactor gas extraction system of chemical industry.
Background technology
The nickel shot dissolution reactor is a kind of reactor of all being participated in mutually by solid, liquid, gas.Because the generation of the gas of hydrogen, acid gas, water vapour and other foul smelling volatile flavors is arranged in the course of reaction, accumulate in the workshop for avoiding hydrogen, eliminate hydrogen explosion hidden danger, normally used is open reactor, carries out in the place preferably at ventilation condition; Like this, certainly will cause the gas of acid gas, water vapour and other foul smelling volatile flavors directly to enter atmosphere, contaminated air; Simultaneously, thermal loss is also very big in the course of reaction, causes the energy consumption of LU weight nickel to increase.
Summary of the invention
The utility model technical problem to be solved provides a kind of orderly discharging of hydric safe that reaction is produced, and acid gas and foul odour gas use alkali lye to reclaim, and water vapour obtains the nickel shot dissolution reactor gas extraction system of condensation reuse.
The utility model solves the technical scheme that its technical problem adopted: a kind of nickel shot dissolution reactor gas extraction system; Said scrubbing tower top is connected with Venturi tube through pipeline, and said wash tower bottoms end is connected with the wash cycle groove through pipeline, is filled with Pall ring in the said scrubbing tower; Be provided with the drip washing shower nozzle in the said scrubbing tower; Said wash cycle groove is connected with the cleaning circulation pump left side through pipeline, and said cleaning circulation pump right side is connected with the drip washing shower nozzle through pipeline, and said wash cycle groove is provided with second exhaust outlet and is connected with Venturi tube through pipeline; Said scrubbing tower is connected with graphite condenser through pipeline; The other reactor that is provided with of said graphite condenser, said reactor head are provided with first exhaust outlet and are connected with the graphite condenser bottom through pipeline, and said reactor head is provided with emergent exhaust outlet and is connected with emergent water sealed tank through pipeline; Said reactor is provided with refluxing opening, and said refluxing opening is connected with graphite condenser through pipeline.
After adopting said structure; Be characterized in: under the normal reaction situation; Gas gets into graphite condenser from first exhaust outlet through pipeline; Emergent exhaust outlet just just works under the emergency when reactor pressure surpasses 50 centimeter water columns, and at this moment reactor tail gas also gets into water sealed tank from emergent exhaust outlet through piping and directly enters atmosphere in through the exhaust outlet discharging.
At first through the graphite condenser cooling, the water vapour that includes and a part of acid gas obtain a part of sour water through supercooling to gas, get into reactor through pipeline from refluxing opening in the reactor; Other hydrogen, foul gas and remaining a part of acid gas get into scrubbing tower; In the washing absorption of scrubbing tower, make acid gas and foul gas and alkali reaction in the gas, only surplus hydrogen in the last gas through sig water and Pall ring; Draw the entering Venturi tube from scrubbing tower top; Mix diluent gas, safety dumping atmosphere with a large amount of air of blower fan input.
The negative pressure of Venturi tube generation here is the draft of whole gas blow-off system; Make acid gas, water vapour in the tail gas obtain reasonable reuse; Foul gas and few part acid gas obtain absorption, have eliminated the pollution to environment, and flammable hydrogen obtains safe and orderly discharging.
Description of drawings
Below in conjunction with accompanying drawing and embodiment the utility model is further specified.
Fig. 1 is the structural representation of the utility model.
Among the figure: 1. scrubbing tower, 2. Venturi tube, 3. washing cannelure, 4. Pall ring, 5. drip washing shower nozzle, 6. cleaning circulation pump, 7. graphite condenser, 8. first exhaust outlet, 9. reactor, 10. emergent exhaust outlet, 11. emergent water sealed tanks, 12. blower fans, 13. refluxing openings, 14. second exhaust outlets.
The specific embodiment
A kind of nickel shot dissolution reactor gas extraction system shown in Figure 1; Comprise scrubbing tower 1, said scrubbing tower 1 top is connected with Venturi tube 2 through pipeline, and said scrubbing tower 1 bottom end is connected with wash cycle groove 3 through pipeline; Be filled with Pall ring 4 in the said scrubbing tower 1; Be provided with drip washing shower nozzle 5 in the said scrubbing tower 1, said wash cycle groove 3 is connected with cleaning circulation pump 6 left sides through pipeline, and said cleaning circulation pump 6 right sides are connected with drip washing shower nozzle 5 through pipeline; Said wash cycle groove 3 is provided with second exhaust outlet 14 and is connected with Venturi tube 2 through pipeline; Said scrubbing tower 1 is connected with graphite condenser 7 through pipeline, the said graphite condenser 7 other reactors 9 that are provided with, and said reactor 9 tops are provided with first exhaust outlet 8 and are connected with graphite condenser 7 bottoms through pipeline; Said reactor 9 tops are provided with anxious exhaust outlet 10 and are connected with emergent water sealed tank 11 through pipeline; Said Venturi tube 2 is connected with blower fan 12 through pipeline, and said reactor 9 is provided with refluxing opening 13, and said refluxing opening 13 is connected with graphite condenser 7 through pipeline.
After adopting said structure, be characterized in: under the normal reaction situation, produce draft by negative pressure in the Venturi tube 2; Make the gas that produces in the reactor 9 get into graphite condenser 7 condensations from first exhaust outlet 8 through pipeline, condensed sour water flows back to through pipeline, gets into reactor 9 reuses from refluxing opening 13; Remaining gas then gets into scrubbing tower 1, and cleaning circulation pump 6 starts, and is sprayed in the scrubbing tower 1 through drip washing shower nozzle 5 from washing cannelure 3 interior extraction alkali lye gas is washed; And be filled with Pall ring 4 in the scrubbing tower 1, with the washing adsorption effect of increase alkali lye, in the washing process to acid gas and foul gas; Alkali lye is back in the wash cycle groove 3 through pipeline, and the portion gas of carrying secretly in the alkali lye is introduced Venturi tube 2 from second exhaust outlet 14 through pipeline, after washing; Only surplus hydrogen in the scrubbing tower 1 is introduced Venturi tube 2 by the negative pressure that Venturi tube 2 produces, and blower fan 12 starts; To a large amount of air of Venturi tube 2 inputs, make the hydrogen in the Venturi tube 2 obtain dilution and enter atmosphere, when reactor 9 internal pressures surpass 50 centimeter water columns; Gas is in through exhaust outlet 8 dischargings in the reactor 9; Also can get into emergent water sealed tank 11 through pipeline from emergent exhaust outlet 10 and directly enter atmosphere, make that acid gas, the water vapour in the tail gas obtains reasonable reuse, foul gas and few part acid gas obtain absorption; Eliminated the pollution to environment, flammable hydrogen obtains safe and orderly discharging.

Claims (2)

1. nickel shot dissolution reactor gas extraction system; Comprise scrubbing tower (1); It is characterized in that: said scrubbing tower (1) top is connected with Venturi tube (2) through pipeline; Said scrubbing tower (1) bottom end is connected with wash cycle groove (3) through pipeline, is filled with Pall ring (4) in the said scrubbing tower (1), is provided with drip washing shower nozzle (5) in the said scrubbing tower (1); Said wash cycle groove (3) is connected with cleaning circulation pump (6) left side through pipeline; Said cleaning circulation pump (6) right side is connected with drip washing shower nozzle (5) through pipeline, and said wash cycle groove (3) is provided with second exhaust outlet (14) and is connected with Venturi tube (2) through pipeline, and said scrubbing tower (1) is connected with graphite condenser (7) through pipeline; The other reactor (9) that is provided with of said graphite condenser (7); Said reactor (9) top is provided with first exhaust outlet (8) and is connected with graphite condenser (7) bottom through pipeline, and said reactor (9) top is provided with anxious exhaust outlet (10) and is connected with emergent water sealed tank (11) through pipeline, and said Venturi tube (2) is connected with blower fan (12) through pipeline.
2. nickel shot dissolution reactor gas extraction system according to claim 1 is characterized in that: said reactor (9) is provided with refluxing opening (13), and said refluxing opening (13) is connected with graphite condenser (7) through pipeline.
CN2012200224973U 2012-01-18 2012-01-18 Exhaust system for nickel particle dissolving reactor Expired - Fee Related CN202410640U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2012200224973U CN202410640U (en) 2012-01-18 2012-01-18 Exhaust system for nickel particle dissolving reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2012200224973U CN202410640U (en) 2012-01-18 2012-01-18 Exhaust system for nickel particle dissolving reactor

Publications (1)

Publication Number Publication Date
CN202410640U true CN202410640U (en) 2012-09-05

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2012200224973U Expired - Fee Related CN202410640U (en) 2012-01-18 2012-01-18 Exhaust system for nickel particle dissolving reactor

Country Status (1)

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CN (1) CN202410640U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110252118A (en) * 2019-07-02 2019-09-20 李召 It is a kind of for handling the filtering separation device of mercurous industrial waste gas

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110252118A (en) * 2019-07-02 2019-09-20 李召 It is a kind of for handling the filtering separation device of mercurous industrial waste gas

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120905

Termination date: 20150118

EXPY Termination of patent right or utility model