CN201140031Y - Apparatus for absorbing alkaline air in off-gas of copper liquid - Google Patents
Apparatus for absorbing alkaline air in off-gas of copper liquid Download PDFInfo
- Publication number
- CN201140031Y CN201140031Y CNU2007200929367U CN200720092936U CN201140031Y CN 201140031 Y CN201140031 Y CN 201140031Y CN U2007200929367 U CNU2007200929367 U CN U2007200929367U CN 200720092936 U CN200720092936 U CN 200720092936U CN 201140031 Y CN201140031 Y CN 201140031Y
- Authority
- CN
- China
- Prior art keywords
- absorption tower
- gas
- ammonia
- copper liquid
- liquid
- 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
- 239000007788 liquid Substances 0.000 title claims abstract description 30
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 title claims abstract description 20
- 229910052802 copper Inorganic materials 0.000 title claims abstract description 20
- 239000010949 copper Substances 0.000 title claims abstract description 20
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 59
- 238000010521 absorption reaction Methods 0.000 claims abstract description 40
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 28
- 238000012856 packing Methods 0.000 claims abstract description 6
- 238000006073 displacement reaction Methods 0.000 claims description 5
- 230000002745 absorbent Effects 0.000 abstract description 3
- 239000002250 absorbent Substances 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000002485 combustion reaction Methods 0.000 abstract description 2
- 238000005406 washing Methods 0.000 abstract description 2
- 238000010926 purge Methods 0.000 abstract 4
- 239000007789 gas Substances 0.000 description 19
- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Landscapes
- Gas Separation By Absorption (AREA)
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a device capable of absorbing ammonia gas in purge gas by copper liquid, which comprises an absorption tower and a gas-liquid separator, wherein the upper portion of the absorption tower is connected with a pump body, the bottom portion of the absorption tower is equipped with a gas inlet and the side wall of the absorption tower is equipped with a liquid outlet. The absorption tower of the device is connected with the pump body, the renewable copper liquid is used as a absorbent and sent into the absorption tower from the top portion of the absorption tower by the pump body, purge gas which is richly contained with ammonia gas and comes from an ammonia storing tank in synthetic ammonia production enters the absorption tower from the bottom portion of the absorption tower, and contacts with copper liquid in countercurrent form sent by the pump body on the packing layer inside the absorption tower. After absorbing, the copper liquid removes harmful gas such as CO in purge gas and then is sent to the next system to use. The purge gas being absorbed contains only about 0.8% ammonia gas, which can be directly sent to a blower and used for combustion. The device has simple structure and high energy utilizing rate, is free of washing process, and greatly saves energy.
Description
Technical field
The utility model relates to a kind of ammonia retracting device, relates in particular to the device that a kind of copper liquid absorbs ammonia in the off-gas.
Background technology
The content of ammonia is generally about 55% in the off-gas in the ammonia storage tank of chemical plant synthesis ammonia system, at present, ammonia enterprises such as most of chemical fertilizer factories are directly sent into off-gas in the blowing-out gas combustion furnace, ammonia is not reclaimed, the enterprise that has directly is discharged into this part gas in the atmosphere, not only caused waste, and severe contamination environment.
The utility model content
The purpose of this utility model is to provide a kind of copper liquid to absorb the device of ammonia in the off-gas, with the ammonia in its off-gas of effective recovery.
To achieve these goals, the technical solution of the utility model has adopted a kind of copper liquid to absorb the device of ammonia in the off-gas, comprises absorption tower, gas-liquid separator, is connected with a pump housing on top, absorption tower, be provided with air inlet in the bottom, absorption tower, sidewall is provided with liquid outlet.
The described pump housing is a plunger displacement pump.
Described separator is connected with the top on absorption tower by pipeline.
In the absorption tower, be provided with packing layer.
Be connected with a pump housing on the absorption tower of the present utility model, copper liquid after the regeneration is as absorbent, be admitted in the absorption tower from the top, absorption tower by the pump housing, the off-gas that is rich in ammonia that ammonia storage tank in the Ammonia Production comes is entered in the absorption tower by the bottom, absorption tower, the copper liquid counter current contacting that the packing layer in the absorption tower and the pump housing are sent here, after copper liquid after the absorption is removed pernicious gases such as CO in the off-gas, be admitted to the utilization of next system, ammonia only is about 0.8% in the off-gas after the absorption, directly delivers to blowing-out gas and uses for burning.Of the present utility model simple in structure, the capacity usage ratio height, and do not have the washing process, saved the energy greatly.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
The specific embodiment
As shown in Figure 1, copper liquid of the present utility model absorbs the device of ammonia in the off-gas, comprises absorption tower 1, gas- liquid separator 2, and 1 top is connected with a plunger displacement pump 3 on the absorption tower, and 1 bottom is provided with air inlet 4 on the absorption tower, and sidewall is provided with liquid outlet 5.Gas-liquid separator 2 is connected by the top of pipeline 6 with absorption tower 1, is provided with packing layer 7 in absorption tower 1.
Copper liquid after the regeneration of the utility model usefulness is as absorbent, be admitted in the absorption tower 1 from 1 top, absorption tower by plunger displacement pump 3, the off-gas that is rich in ammonia that ammonia storage tank in the Ammonia Production is sent here is entered in the absorption tower 1 by the air inlet 4 of 1 bottom, absorption tower, the copper liquid counter current contacting that packing layer 7 in absorption tower 1 and plunger displacement pump 3 are sent here, copper liquid behind the absorption ammonia enters into a next system and is utilized, only contain ammonia about 0.8% in the off-gas after the absorption in the gas of ammonia behind gas-liquid separator 2, directly delivered to blowing-out gas and use for burning.
Claims (4)
1, a kind of copper liquid absorbs the device of ammonia in the off-gas, it is characterized in that: comprise absorption tower, gas-liquid separator, be connected with a pump housing on top, absorption tower, be provided with air inlet in the bottom, absorption tower, sidewall is provided with liquid outlet.
2, copper liquid according to claim 1 absorbs the device of ammonia in the off-gas, and it is characterized in that: the described pump housing is a plunger displacement pump.
3, copper liquid according to claim 1 absorbs the device of ammonia in the off-gas, and it is characterized in that: described separator is connected with the top on absorption tower by pipeline.
4, absorb the device of ammonia in the off-gas according to arbitrary described copper liquid among the claim 1-3, it is characterized in that: in the absorption tower, be provided with packing layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200929367U CN201140031Y (en) | 2007-11-27 | 2007-11-27 | Apparatus for absorbing alkaline air in off-gas of copper liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200929367U CN201140031Y (en) | 2007-11-27 | 2007-11-27 | Apparatus for absorbing alkaline air in off-gas of copper liquid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201140031Y true CN201140031Y (en) | 2008-10-29 |
Family
ID=40067748
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007200929367U Expired - Fee Related CN201140031Y (en) | 2007-11-27 | 2007-11-27 | Apparatus for absorbing alkaline air in off-gas of copper liquid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201140031Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102179135A (en) * | 2011-04-26 | 2011-09-14 | 苏州利盛化工设备有限公司 | Ammonia absorption device |
| CN102583439A (en) * | 2012-02-08 | 2012-07-18 | 浠水县福瑞德化工有限责任公司 | Available gas recovery method in ammonia synthesis process |
| CN113181764A (en) * | 2021-04-12 | 2021-07-30 | 南通大学 | Ammonia gas treatment device for detecting nitrogen oxides of SCR (Selective catalytic reduction) denitration device and working method thereof |
-
2007
- 2007-11-27 CN CNU2007200929367U patent/CN201140031Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102179135A (en) * | 2011-04-26 | 2011-09-14 | 苏州利盛化工设备有限公司 | Ammonia absorption device |
| CN102179135B (en) * | 2011-04-26 | 2013-04-10 | 苏州利盛化工设备有限公司 | Ammonia absorption device |
| CN102583439A (en) * | 2012-02-08 | 2012-07-18 | 浠水县福瑞德化工有限责任公司 | Available gas recovery method in ammonia synthesis process |
| CN102583439B (en) * | 2012-02-08 | 2013-07-24 | 浠水县福瑞德化工有限责任公司 | Available gas recovery method in ammonia synthesis process |
| CN113181764A (en) * | 2021-04-12 | 2021-07-30 | 南通大学 | Ammonia gas treatment device for detecting nitrogen oxides of SCR (Selective catalytic reduction) denitration device and working method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100490943C (en) | Treatment device for waste gas containing nitrogen oxides | |
| CN201333374Y (en) | Device capable of collecting carbon dioxide contained in flue gases of power plant through ammonia by utilizing void tower | |
| CN101314102A (en) | Carbon dioxide capture method and device in flue gas of coal-fired power plant | |
| CN102500323B (en) | Modified active carbon desulfurizer and preparation method thereof and treatment method of hydrogen sulfide waste gas | |
| CN204973462U (en) | Continuous flow purifier of intermittent type formula reation kettle unloading waste gas | |
| CN107088355B (en) | Multistage waste gas treatment device and method using solar energy as power | |
| CN203043799U (en) | Acid mist purification tower | |
| CN201140031Y (en) | Apparatus for absorbing alkaline air in off-gas of copper liquid | |
| CN102179134A (en) | Ammonia water recovery device | |
| Paolini et al. | Water scrubbing for biogas upgrading: developments and innovations | |
| CN201873655U (en) | Biomass methane refining system | |
| CN107174931B (en) | High-efficient flue gas processing apparatus of power is regarded as to ethernet | |
| CN101905114B (en) | High purification method of industrial tail gas containing oxynitride | |
| CN202343087U (en) | Efficient waste gas neutralizing tower | |
| CN103357260A (en) | Integrated flue gas desulfurization and denitrification process using ferrous complexing agent to enhance urea | |
| CN204735101U (en) | Efficient ammonia nitrogen tail gas absorbing device | |
| CN105344224A (en) | Styrene exhaust gas treatment method | |
| CN202087187U (en) | Ammonia water recovery device | |
| CN201768475U (en) | Vacuum pump waste gas absorption and emission reduction device | |
| CN203507805U (en) | Flue gas desulfurization and denitration tower | |
| CN214528878U (en) | Biogas filtering and purifying system in co-production of biogas and organic fertilizer by straw, livestock and poultry manure | |
| CN203389527U (en) | Low-temperature multi-effect flue gas treatment device | |
| CN214182532U (en) | A device for solving the emission of greenhouse gases from catalytic hydrolysis of urea | |
| CN210934112U (en) | Carbon dioxide trapping device | |
| CN202478634U (en) | Device for processing acid mist |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: LINGBAO XINGHUA CHEMICAL CO., LTD. Free format text: FORMER OWNER: LINGBAO CITY JINYUAN MINING CO., LTD. Effective date: 20110127 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 472500 NO.20, JINCHENG AVENUE, LINGBAO CITY, HE NAN PROVINCE TO: 472500 MIDDLE SECTION OF DINGYUAN ROAD, LINGBAO CITY, HE NAN PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20110127 Address after: 472500 Lingbao Road, Lingbao City, Henan Province Patentee after: Lingbao Xinghua Chemical Industy Co., Ltd. Address before: 472500, Jincheng Road, Lingbao City, Henan Province, No. 20 Patentee before: Lingbao City Jinyuan Mining Co., Ltd. |
|
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20081029 Termination date: 20121127 |