CN202638240U - Ammonia gas recovery device - Google Patents

Ammonia gas recovery device Download PDF

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Publication number
CN202638240U
CN202638240U CN2012202879113U CN201220287911U CN202638240U CN 202638240 U CN202638240 U CN 202638240U CN 2012202879113 U CN2012202879113 U CN 2012202879113U CN 201220287911 U CN201220287911 U CN 201220287911U CN 202638240 U CN202638240 U CN 202638240U
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CN
China
Prior art keywords
absorption tower
gas absorption
ammonia gas
circulating pump
amine 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
CN2012202879113U
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Chinese (zh)
Inventor
安继军
李雄
袁维
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.)
HUNAN HUIZHENG ENVIRONMENTAL SCIENCE AND TECHNOLOGY DEVELOPMENT Co Ltd
Original Assignee
HUNAN HUIZHENG ENVIRONMENTAL SCIENCE AND TECHNOLOGY DEVELOPMENT 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
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Application filed by HUNAN HUIZHENG ENVIRONMENTAL SCIENCE AND TECHNOLOGY DEVELOPMENT Co Ltd filed Critical HUNAN HUIZHENG ENVIRONMENTAL SCIENCE AND TECHNOLOGY DEVELOPMENT Co Ltd
Priority to CN2012202879113U priority Critical patent/CN202638240U/en
Application granted granted Critical
Publication of CN202638240U publication Critical patent/CN202638240U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses an ammonia gas recovery device, which comprises a primary ammonia gas absorption tower, a secondary ammonia gas absorption tower, a circulating water tank, a circulating pump I, a circulating pump II and manholes, wherein the primary ammonia gas absorption tower is connected with the secondary ammonia gas absorption tower through an ammonia gas conveying pipe; the secondary ammonia gas absorption tower is connected with the circulating pump II through a circulating pipeline; the circulating pump II and the circulating pump I are connected to the two ends of the circulating water tank through pipelines; the circulating pump I is connected with the primary ammonia gas absorption tower through a circulating pipeline; and both the primary ammonia gas absorption tower and the secondary ammonia gas absorption tower are provided with two manholes. The ammonia gas recovery device has the advantages of high performance price ratio, long service life, small equipment floor area, low price and good absorption effect. An entire piece of equipment has excellent chemical corrosion resistance, and does not damage strongly-oxidative materials such as inorganic compounds including acidic, alkaline and saline solutions till the temperature reaches 100 DEG C.

Description

A kind of ammonia recycling device
Technical field
The utility model relates to retracting device, is specially a kind of ammonia recycling device.
Background technology
A kind of ammonia recycling device is applied to the retracting device that high-concentration ammonia nitrogenous wastewater is processed rear ammonia.During high-concentration ammonia nitrogenous wastewater is processed, ammonia passes through gas and water separator, make ammonia escape dewatered constraint, blown in the air, but ammonia has corrosion and spread effect to the skin histology of contact, can absorb the moisture in the skin histology, makes the histone sex change, and make the tissue fat saponification, destroy membrane structure.The solubility of ammonia is high, stimulates and corrosiveness so mainly the upper respiratory tract of animal or human's body is had, often be attracted to mucocutaneous and the eye conjunctiva on, stimulate and inflammation thereby produce.Can benumb respiratory tract cilium and infringement mucous epithelium tissue, make pathogenic microorganism be easy to invade, weaken human body to the resistance of disease.Ammonia sucks human body with gas form usually, and ammonia easily enters blood by alveolar after being inhaled into lung, is combined with hemoglobin, destroys fortune oxygen function.So it is necessary that Ammonia recovery is recycled, and also is feasible.
The utility model content
The technical problem that the utility model solves is to provide a kind of ammonia recycling device, to solve the shortcoming in the above-mentioned background technology.
The technical problem that the utility model solves realizes by the following technical solutions:
A kind of ammonia recycling device, comprise primary amine gas absorption tower, secondary amine gas absorption tower, cyclic water tank, circulating pump one, circulating pump two and hand-hole, be connected by the ammonia carrier pipe between described primary amine gas absorption tower and the secondary amine gas absorption tower, be connected by circulating line between described secondary amine gas absorption tower and the circulating pump two, described circulating pump two and circulating pump one are connected to the two ends of described cyclic water tank by pipeline, described circulating pump one is connected with primary amine gas absorption tower by circulating line.Be equipped with two hand-holes on primary amine gas absorption tower and the secondary amine gas absorption tower.
Described secondary amine gas also is provided with blowdown stack and rainhat on the absorption tower, and described blowdown stack is installed on the described secondary amine gas absorption tower, and described rainhat is installed in the top of described blowdown stack.
Described cyclic water tank also is provided with mouth for subsequent use, glass-tube liquid level meter and running water entrance, and described mouth for subsequent use is located at the top of described cyclic water tank, and described glass-tube liquid level meter and running water entrance are located at the right-hand member of described cyclic water tank.
Also be provided with the weak aqua ammonia delivery pipe on the described circulating line, the bottom of described weak aqua ammonia delivery pipe also is connected with sampling nozzle.
Primary amine gas absorption tower, secondary amine gas are provided with two-layer spray system in the absorption tower.
The set-up mode of circulating pump one, circulating pump two, circulating line has guaranteed the concentration requirement of weak aqua ammonia.
Primary amine gas absorption tower, secondary amine gas absorption tower and cyclic water tank are an integral body.
Beneficial effect:
The utility model cost performance is high, and physical life is long.Equipment takes up an area little, cheap, good absorbing effect.Integral device all has good chemical resistance, no matter remove outside the material of strong oxidizing property for inorganic compound acid, alkali, salting liquid, temperature until 100 ℃ all to it without destruction.
Description of drawings
Fig. 1 is a kind of ammonia recycling device schematic diagram.
The specific embodiment
For technological means, creation characteristic that the utility model is realized, reach purpose and effect is easy to understand, below in conjunction with concrete diagram, further set forth the utility model.
A kind of ammonia recycling device, comprise primary amine gas absorption tower 1, secondary amine gas absorption tower 2, cyclic water tank 3, circulating pump 1, circulating pump 28 and hand-hole 12, be connected by ammonia carrier pipe 17 between described primary amine gas absorption tower 1 and the secondary amine gas absorption tower 2, be connected by circulating line 15 between described secondary amine gas absorption tower 2 and the circulating pump 28, described circulating pump 28 and circulating pump 1 are connected to the two ends of described cyclic water tank 3 by pipeline, described circulating pump 1 is connected with primary amine gas absorption tower 1 by circulating line 15.Be equipped with two hand-holes 12 on primary amine gas absorption tower 1 and the secondary amine gas absorption tower 2.
Also be provided with blowdown stack 5 and rainhat 6 on the described secondary amine gas absorption tower 2, described blowdown stack 5 is installed on the described secondary amine gas absorption tower 2, and described rainhat 6 is installed in the top of described blowdown stack 5.
Described cyclic water tank 3 also is provided with mouth 4 for subsequent use, glass-tube liquid level meter 14 and running water entrance 9, described for subsequent use mouthful 4 top that is located at described cyclic water tank 3, and described glass-tube liquid level meter 14 and running water entrance 9 are located at the right-hand member of described cyclic water tank 3.
Also be provided with weak aqua ammonia delivery pipe 10 on the described circulating line 15, the bottom of described weak aqua ammonia delivery pipe 10 also is connected with sampling nozzle 11.
During enforcement:
At first cyclic water tank 3 is passed into running water, again waste gas is entered pipe 16 from ammonia and enters primary amine gas absorption tower 1, ON cycle pump primary amine gas absorption tower one 7 this moment 1 interior two-stage spray system and automatically open, absorb incomplete free ammonia by ammonia conveyance conduit 17 to secondary amine gas absorption tower 2, ON cycle pump secondary amine gas absorption tower 28 this moment 2 brings into play effects and guarantees that free ammonia all is absorbed by liquid absorption.Gas up to standard is discharged in the atmosphere by blowdown stack 5.
Above demonstration and described basic principle of the present utility model and principal character and advantage of the present utility model; the technical staff of the industry should understand; the utility model is not restricted to the described embodiments; that describes in above-described embodiment and the specification just illustrates principle of the present utility model; under the prerequisite that does not break away from the utility model spirit and scope; the utility model also has various changes and modifications; these changes and improvements all fall in claimed the utility model scope, and the claimed scope of the utility model is defined by appending claims and equivalent thereof.

Claims (4)

1. ammonia recycling device, comprise primary amine gas absorption tower, secondary amine gas absorption tower, cyclic water tank, circulating pump one, circulating pump two and hand-hole, it is characterized in that, be connected by the ammonia carrier pipe between described primary amine gas absorption tower and the secondary amine gas absorption tower, be connected by circulating line between described secondary amine gas absorption tower and the circulating pump two, described circulating pump two and circulating pump one are connected to the two ends of described cyclic water tank by pipeline, described circulating pump one is connected with primary amine gas absorption tower by circulating line, is equipped with two hand-holes on primary amine gas absorption tower and the secondary amine gas absorption tower.
2. described a kind of ammonia recycling device according to claim 1, it is characterized in that, described secondary amine gas also is provided with blowdown stack and rainhat on the absorption tower, and described blowdown stack is installed on the described secondary amine gas absorption tower, and described rainhat is installed in the top of described blowdown stack.
3. described a kind of ammonia recycling device according to claim 1, it is characterized in that, described cyclic water tank also is provided with mouth for subsequent use, glass-tube liquid level meter and running water entrance, described mouth for subsequent use is located at the top of described cyclic water tank, and described glass-tube liquid level meter and running water entrance are located at the right-hand member of described cyclic water tank.
4. described a kind of ammonia recycling device according to claim 1 is characterized in that, also be provided with the weak aqua ammonia delivery pipe on the described circulating line, the bottom of described weak aqua ammonia delivery pipe also is connected with sampling nozzle.
CN2012202879113U 2012-06-19 2012-06-19 Ammonia gas recovery device Expired - Fee Related CN202638240U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2012202879113U CN202638240U (en) 2012-06-19 2012-06-19 Ammonia gas recovery device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2012202879113U CN202638240U (en) 2012-06-19 2012-06-19 Ammonia gas recovery device

Publications (1)

Publication Number Publication Date
CN202638240U true CN202638240U (en) 2013-01-02

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2012202879113U Expired - Fee Related CN202638240U (en) 2012-06-19 2012-06-19 Ammonia gas recovery device

Country Status (1)

Country Link
CN (1) CN202638240U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104117267A (en) * 2014-08-11 2014-10-29 乳山市日晟机械制造有限公司 Ammonia gas film-falling absorption device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104117267A (en) * 2014-08-11 2014-10-29 乳山市日晟机械制造有限公司 Ammonia gas film-falling absorption device

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GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130102

Termination date: 20150619

EXPY Termination of patent right or utility model