CN203816458U - Equipment comprising ammonia water storage tank provided with ammonia gas washing device - Google Patents
Equipment comprising ammonia water storage tank provided with ammonia gas washing device Download PDFInfo
- Publication number
- CN203816458U CN203816458U CN201320749754.8U CN201320749754U CN203816458U CN 203816458 U CN203816458 U CN 203816458U CN 201320749754 U CN201320749754 U CN 201320749754U CN 203816458 U CN203816458 U CN 203816458U
- Authority
- CN
- China
- Prior art keywords
- ammonia
- ammoniacal liquor
- absorption tower
- storage tank
- water storage
- 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
Links
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims abstract description 73
- 235000011114 ammonium hydroxide Nutrition 0.000 title claims abstract description 47
- 238000003860 storage Methods 0.000 title abstract description 7
- 238000005406 washing Methods 0.000 title abstract description 7
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 title abstract 8
- 238000010521 absorption reaction Methods 0.000 claims abstract description 27
- 229910021529 ammonia Inorganic materials 0.000 claims description 34
- 239000007921 spray Substances 0.000 claims description 8
- 238000004140 cleaning Methods 0.000 claims description 5
- 230000008676 import Effects 0.000 claims description 5
- 238000012856 packing Methods 0.000 claims description 5
- 230000010354 integration Effects 0.000 claims description 4
- 239000000463 material Substances 0.000 abstract description 4
- 230000007704 transition Effects 0.000 abstract description 2
- 238000007599 discharging Methods 0.000 abstract 1
- 238000013461 design Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
Abstract
The utility model discloses equipment comprising an ammonia water storage tank provided with an ammonia gas washing device. The equipment comprises an ammonia gas absorption tower and an ammonia water storage tank, wherein the ammonia water storage tank is mounted at the bottom of the ammonia gas absorption tower and integrally formed with the ammonia gas absorption tower; an ammonia water output pipe is arranged at the bottom of the ammonia water storage tank and connected with a washing shower pipe by virtue of a circulating washing pump; the washing shower pipe is mounted at the upper part of the ammonia gas absorption tower; an ammonia water charging and discharging pipe and a gas charging pipe are respectively arranged on the ammonia water storage tank; an exhausting pipe is arranged at the top of the ammonia gas absorption tower. The equipment disclosed by the utility model is compact in overall structure and the use of lots of transition materials is avoided, so the materials are saved and the cost is lowered.
Description
Technical field
The utility model is specifically related to the equipment of the subsidiary ammonia wash mill of a kind of ammoniacal liquor basin.
Background technology
After the tail gas that contains ammonia generally need to be processed, just can be discharged in atmosphere, in ammonia processing procedure, generally need to wash it, by the ammoniacal liquor basin of the ammoniacal liquor storage after washing, so both purify air, also can, to Ammonia recovery utilization, save production cost simultaneously; The absorption tower of existing processing ammonia is arranged with the ammoniacal liquor basin point of depositing ammoniacal liquor, and therefore, field apparatus arrangement space is large, the occupation of land that equipment needs is large, and some connecting pipes of intermediate demand, even set up delivery pump, cost compare is high, operates more complicated simultaneously.
Utility model content
For addressing the above problem, the utility model object is in the equipment that the subsidiary ammonia wash mill of ammoniacal liquor basin that a kind of cost is low, simple to operate and recovering effect is good is provided.
For achieving the above object, the technical scheme that the utility model adopts is:
The equipment of the subsidiary ammonia wash mill of ammoniacal liquor basin of the present utility model, comprises ammonia absorption tower and ammoniacal liquor basin; Described ammoniacal liquor basin is arranged on bottom, ammonia absorption tower, and is made into integration with ammonia absorption tower; Described ammoniacal liquor tank bottom is provided with ammoniacal liquor efferent duct, and described ammoniacal liquor efferent duct is connected with wash spray pipe by circulation cleaning pump; Described wash spray pipe is arranged on top, ammonia absorption tower; On described ammoniacal liquor basin, be respectively arranged with ammoniacal liquor and import and export pipe and gas introduction tube; Top, described ammonia absorption tower is provided with blast pipe.
As preferably, in described ammonia absorption tower, be also provided with filter packing layer.
Beneficial effect:
Compared with prior art, the equipment of the subsidiary ammonia wash mill of ammoniacal liquor basin of the present utility model, is directly set together ammoniacal liquor basin and ammonia absorption tower, directly makes an entirety; Compact overall structure, a lot of transition materials have been reduced in centre, save material, reduce costs; Simultaneously, because ammoniacal liquor basin and ammonia absorption tower are made into integration, reduce to a great extent the floor space of equipment.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
1-ammonia absorption tower; 2-ammoniacal liquor basin; 3-ammoniacal liquor efferent duct, 4-circulation cleaning pump; 5-wash spray pipe; 6-ammoniacal liquor imports and exports pipe; 7-gas introduction tube; 8-filter packing layer; 9-blast pipe.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is further described:
The equipment of the subsidiary ammonia wash mill of ammoniacal liquor basin of the present utility model, comprises ammonia absorption tower 1 and ammoniacal liquor basin 2; Described ammoniacal liquor basin 2 is arranged on 1 bottom, ammonia absorption tower, and is made into integration with ammonia absorption tower 1; Described ammoniacal liquor basin 2 bottoms are provided with ammoniacal liquor efferent duct 3, and described ammoniacal liquor efferent duct 3 is connected with wash spray pipe 5 by circulation cleaning pump 4; Described wash spray pipe 5 is arranged on 1 top, ammonia absorption tower; On described ammoniacal liquor basin 2, be respectively arranged with ammoniacal liquor and import and export pipe 6 and gas introduction tube 7; Top, described ammonia absorption tower is provided with blast pipe 9.
In described ammonia absorption tower 1, be also provided with filter packing layer 8.
The course of work of the present utility model is: ammoniacal liquor can import and export pipe by ammoniacal liquor and directly introduces or draw; Ammonia circulates by circulation cleaning pump: wash spray pipe washs ammonia after mixing by gas introduction tube and ammoniacal liquor, and ammoniacal liquor is got back to ammoniacal liquor basin by filter packing layer; Tail gas after purification and washing is discharged in atmosphere by blast pipe.
Embodiment recited above is described preferred embodiment of the present utility model, not design of the present utility model and scope is limited.Do not departing under the prerequisite of the utility model design concept; various modification and improvement that this area ordinary person makes the technical solution of the utility model; all should drop into protection domain of the present utility model; the technology contents of the utility model request protection, has all been documented in claims.
Claims (1)
1. an equipment for the subsidiary ammonia wash mill of ammoniacal liquor basin, comprises ammonia absorption tower and ammoniacal liquor basin; It is characterized in that: described ammoniacal liquor basin is arranged on bottom, ammonia absorption tower, and be made into integration with ammonia absorption tower; Described ammoniacal liquor tank bottom is provided with ammoniacal liquor efferent duct, and described ammoniacal liquor efferent duct is connected with wash spray pipe by circulation cleaning pump; Described wash spray pipe is arranged on top, ammonia absorption tower; On described ammoniacal liquor basin, be respectively arranged with ammoniacal liquor and import and export pipe and gas introduction tube; Top, described ammonia absorption tower is provided with blast pipe; In described ammonia absorption tower, be also provided with filter packing layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320749754.8U CN203816458U (en) | 2013-11-22 | 2013-11-22 | Equipment comprising ammonia water storage tank provided with ammonia gas washing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320749754.8U CN203816458U (en) | 2013-11-22 | 2013-11-22 | Equipment comprising ammonia water storage tank provided with ammonia gas washing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203816458U true CN203816458U (en) | 2014-09-10 |
Family
ID=51472002
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320749754.8U Expired - Fee Related CN203816458U (en) | 2013-11-22 | 2013-11-22 | Equipment comprising ammonia water storage tank provided with ammonia gas washing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203816458U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105126546A (en) * | 2015-08-10 | 2015-12-09 | 大唐环境产业集团股份有限公司 | Ammonia absorption treatment device and method |
| CN108283865A (en) * | 2018-02-08 | 2018-07-17 | 贵州省德邦环保化工有限公司 | Ammonia processing unit |
| CN110665337A (en) * | 2018-07-03 | 2020-01-10 | 山东恒昌圣诚化工股份有限公司 | Ammonia tail gas recovery device |
-
2013
- 2013-11-22 CN CN201320749754.8U patent/CN203816458U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105126546A (en) * | 2015-08-10 | 2015-12-09 | 大唐环境产业集团股份有限公司 | Ammonia absorption treatment device and method |
| CN105126546B (en) * | 2015-08-10 | 2017-09-22 | 大唐环境产业集团股份有限公司 | A kind of ammonia absorption treating device and method |
| CN108283865A (en) * | 2018-02-08 | 2018-07-17 | 贵州省德邦环保化工有限公司 | Ammonia processing unit |
| CN110665337A (en) * | 2018-07-03 | 2020-01-10 | 山东恒昌圣诚化工股份有限公司 | Ammonia tail gas recovery device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140910 Termination date: 20211122 |