CN102179134A - Ammonia water recovery device - Google Patents
Ammonia water recovery device Download PDFInfo
- Publication number
- CN102179134A CN102179134A CN2011101052033A CN201110105203A CN102179134A CN 102179134 A CN102179134 A CN 102179134A CN 2011101052033 A CN2011101052033 A CN 2011101052033A CN 201110105203 A CN201110105203 A CN 201110105203A CN 102179134 A CN102179134 A CN 102179134A
- Authority
- CN
- China
- Prior art keywords
- delivery port
- air inlet
- gas outlet
- absorption tower
- water inlet
- 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.)
- Pending
Links
Images
Landscapes
- Treating Waste Gases (AREA)
Abstract
The invention discloses an ammonia water recovery device, which comprises a gas buffer tank, a vacuum unit connected with the gas buffer tank, a first absorption tower connected with the vacuum unit, an absorption tank connected with the first absorption tower and a water storage tank. Because of multi-stage ammonia absorption and ammonia water recovery, the ammonia water recovery device has good absorption and recovery effects; the concentration of the discharged waste gas after the absorption is not more than 1 mg/m3, and the purification efficiency is not less than 99% and is lower than the Chinese (GB14554-93) odor pollutant comprehensive discharge primary and secondary standards 1.0 mg/m3 and 1.5 mg/m3; and the discharge amount is smaller than or equal to the standard of 4.9 kg/h when the height is 15 m.
Description
Technical field
The present invention relates to a kind of chemical industry equipment, specifically the ammoniacal liquor retracting device.
Background technology
Ammonia, inorganic compound, normal temperature is gas down, the colourless smell that the excitant stench is arranged, soluble in water, be called ammoniacal liquor when ammonia is water-soluble, amino molecule is combined into a hydration ammonia (NH3H2O) with hydrone by the * hydrogen bond, one hydration ammonia can fraction be ionized into ammonium ion and hydroxide ion, so ammoniacal liquor shows alkalescent, can make the phenolphthalein solution look that reddens.Ammonia and acid effect can arrive ammonium salt, ammonia is mainly as refrigerant and produce ammonium salt and nitrogenous fertilizer.In fields such as chemical industry and the desulfurization of non-ferrous metal metallurgy industry, dechlorination, denitrations, contain a large amount of ammonias in the exhaust gas discharged, if it is not effectively handled, will cause severe contamination to environment.Present ammoniacal liquor reclaimer only can reach the minimum standard of country to the absorption of ammonia, have in addition do not reach, therefore environment is seriously influenced.
Summary of the invention
The objective of the invention is the deficiency that exists at prior art, thereby provide a kind of ammonia good absorbing effect, can effectively reclaim the ammoniacal liquor retracting device of ammoniacal liquor better protection environment.
For achieving the above object, the technical solution used in the present invention is a kind of ammoniacal liquor retracting device, the vacuum unit that comprises the gas buffer jar, joins with the gas buffer jar, first absorption tower that joins with the vacuum unit, the adsorption tanks and the cistern that join with first absorption tower; On the gas buffer jar, be provided with first air inlet, first gas outlet, first water inlet and first delivery port, on the vacuum unit, be provided with second air inlet, second gas outlet, second water inlet and second delivery port, on first absorption tower, be provided with the 3rd air inlet, the 3rd gas outlet, the 3rd water inlet, the 3rd delivery port and the 4th delivery port, on adsorption tanks, be provided with the 6th air inlet and escape pipe, on cistern, be provided with the 6th water inlet and the 9th delivery port; Wherein first gas outlet and second air inlet join, second gas outlet and the 3rd air inlet join, the 3rd gas outlet and the 6th air inlet join, and the 3rd water inlet and the 9th delivery port join, and first delivery port, second delivery port, the 3rd delivery port, the 4th delivery port all join with the 6th water inlet.
Better ammonia absorbs and the effect of ammoniacal liquor recovery in order to reach, and this ammoniacal liquor retracting device also comprises second absorption tower and the 3rd absorption tower, and described the 3rd gas outlet joins by second absorption tower and the 3rd absorption tower and the 6th air inlet; On second absorption tower, be provided with the 4th air inlet, the 4th gas outlet, the 4th water inlet, the 5th delivery port and the 6th delivery port, be provided with the 5th air inlet, the 5th gas outlet, the 5th water inlet, the 7th delivery port and the 8th delivery port on the 3rd absorption tower; Described the 3rd gas outlet and the 4th air inlet join, the 4th gas outlet and the 5th air inlet join, the 5th gas outlet and the 6th air inlet join, the 4th water inlet and the 5th water inlet all join with the 9th delivery port, and the 5th delivery port, the 6th delivery port, the 7th delivery port and the 8th delivery port all join with the 6th water inlet.
Also be provided with the 7th gas outlet between described second gas outlet and the 3rd air inlet, described escape pipe is provided with the 7th air inlet, and described the 7th gas outlet and the 7th air inlet join.
For reaching better adsorption effect, described adsorption tanks are absorbent charcoal adsorption tank.
For ensureing gas buffer jar safety, to avoid it to bear and do not live high pressure and explosion, described gas buffer tank wall also is provided with two circle stiffening rings.
Beneficial effect: the present invention is owing to passed through multistage ammonia absorption and ammoniacal liquor recycling, and therefore absorption and recovering effect are fabulous, exhaust gas discharged concentration≤1mg/m after absorbing
3, purification efficiency 〉=99% is lower than China (GB14554-93) odorant pollutant comprehensive discharge standard one-level 1.0mg/m
3Secondary 1.5mg/m
3, during 15 meters of discharge capacitys height smaller or equal to 4.9 kilograms/hour standard.
Description of drawings
Fig. 1 is a structural representation of the present invention.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, further illustrate the present invention, present embodiment is being to implement under the prerequisite with the technical solution of the present invention, should understand these embodiment and only be used to the present invention is described and be not used in and limit the scope of the invention.
As shown in Figure 1, a kind of ammoniacal liquor retracting device, the vacuum unit 2 that comprises gas buffer jar 1, joins with the gas buffer jar, the first absorption tower 3a that joins with vacuum unit 2, the second absorption tower 3b that joins with the first absorption tower 3a, the 3rd absorption tower 3c that joins with the second absorption tower 3b, the absorbent charcoal adsorption tank 4 and the cistern 22 that join with the 3rd absorption tower 3c; On gas buffer jar 1, be provided with first air inlet 5, first gas outlet 6, first water inlet 7 and first delivery port 8, on its outer wall, also be provided with two circle stiffening rings 25, on vacuum unit 2, be provided with second air inlet 9, second gas outlet, 10, second water inlet 11 and second delivery port 12, on the first absorption tower 3a, be provided with the 3rd air inlet 13a, the 3rd gas outlet 14a, the 3rd water inlet 15a, the 3rd delivery port 16a and the 4th delivery port 17a, on the second absorption tower 3b, be provided with the 4th air inlet 13b, the 4th gas outlet 14b, the 4th water inlet 15b, the 5th delivery port 16b and the 6th delivery port 17b, on the 3rd absorption tower 3c, be provided with the 5th air inlet 13c, the 5th gas outlet 14c, the 5th water inlet 15c, the 7th delivery port 16c and the 8th delivery port 17c, on absorbent charcoal adsorption tank 4, be provided with the 6th air inlet 18 and escape pipe 19, on cistern 22, be provided with the 6th water inlet 23 and the 9th delivery port 24, between second gas outlet 10 and the 3rd air inlet 13a, also be provided with the 7th gas outlet 20, on escape pipe 19, be provided with the 7th air inlet 21; Wherein first gas outlet 6 and second air inlet 9 join, second gas outlet 10 and the 3rd air inlet 13a join, the 3rd gas outlet 14a and the 4th air inlet 13b join, the 4th gas outlet 14b and the 5th air inlet 13c join, the 5th gas outlet 14c and the 6th air inlet 18 join, the 3rd water inlet 15a, the 4th water inlet 15b and the 5th water inlet 15c all join with the 9th delivery port 24, first delivery port 8, second delivery port 12, the 3rd delivery port 16a, the 4th delivery port 17a, the 5th delivery port 16b, the 6th delivery port 17b, the 7th delivery port 16c and the 8th delivery port 17c all join with the 6th water inlet 23, and the 7th gas outlet 20 and the 7th air inlet 21 join.
The present invention mainly utilizes hydromechanical relative theory, gas mixes in pipeline with absorption liquid, after mixing with gas, absorption liquid passes through pipeline, at this moment gas-liquid two-phase is big with the tube wall contact-making surface, contact surface liquid constantly obtains cooling, reach efficient chemical exchange reaction, the fierce collision of gas-liquid is so that after gas-liquid fully mixes, along with the gravity effect of liquid falls into cyclic water tank.
Workflow is as follows: the ammonia tail gas of band dust enters in the gas buffer jar under the effect of vacuum, make dust follow gas to separate, pure then ammonia continues to carry out secondary water washing in the water tank that volatilization enters the vacuum unit, because the liquid in the water tank constantly heats up under the ringing of water pump, this moment, ammonia was water insoluble, continuing evaporation and enter first absorption tower, is that absorption liquid absorbs with water.Ammonia in the process that water absorbs along with the raising of absorption strength, the temperature of absorption liquid can be along with rising, in order to ensure assimilation effect, so absorption liquid is fully absorbed with cooling water circulation cooling back, the gas that part does not absorb fully enters second absorption tower to be continued to absorb, the gas that was absorbed subsequently enters the 3rd absorption tower again, this moment, the concentration of ammonia was very low, because gas and liquid are also being absorbed by the water circulation, so volatility is very low, the gas of discharging has been pure air relatively, and entering the final gas of discharging of absorbent charcoal adsorption tank absorption again is pure air basically.When the ammonia concn in first absorption tower reaches capacity, it is squeezed into finished product storage tank, simultaneously the ammoniacal liquor of relative high concentration in second absorption tower is squeezed into and continued in first absorption tower to absorb, the low concentration ammoniacal liquor of the 3rd absorption tower mother liquor tank is squeezed into second absorption tower continue the circulation absorption, in the 3rd absorption tower circulating tank groove, inject clear water and continue to absorb.The circulation that goes round and begins again thus absorbs, and finally reaches recovery ammoniacal liquor, the effect of emission compliance, and promptly the economic benefit of Chuan Zaoing makes environment obtain protection again.
Claims (5)
1. ammoniacal liquor retracting device is characterized in that: the vacuum unit (2) that comprises gas buffer jar (1), joins with the gas buffer jar, first absorption tower (3a) that joins with vacuum unit (2), the adsorption tanks (4) and the cistern (22) that join with first absorption tower (3a); On gas buffer jar (1), be provided with first air inlet (5), first gas outlet (6), first water inlet (7) and first delivery port (8), on vacuum unit (2), be provided with second air inlet (9), second gas outlet (10), second water inlet (11) and second delivery port (12), on first absorption tower (3a), be provided with the 3rd air inlet (13a), the 3rd gas outlet (14a), the 3rd water inlet (15a), the 3rd delivery port (16a) and the 4th delivery port (17a), on adsorption tanks (4), be provided with the 6th air inlet (18) and escape pipe (19), on cistern (22), be provided with the 6th water inlet (23) and the 9th delivery port (24); Wherein first gas outlet (6) join with second air inlet (9), second gas outlet (10) joins with the 3rd air inlet (13a), the 3rd gas outlet (14a) joins with the 6th air inlet (18), the 3rd water inlet (15a) joins with the 9th delivery port (24), and first delivery port (8), second delivery port (12), the 3rd delivery port (16a), the 4th delivery port (17a) all join with the 6th water inlet (23).
2. according to the described a kind of ammoniacal liquor retracting device of claim 1, it is characterized in that: also comprise second absorption tower (3b) and the 3rd absorption tower (3c), described the 3rd gas outlet (14a) joins with the 6th air inlet (18) by second absorption tower (3b) and the 3rd absorption tower (3c); On second absorption tower (3b), be provided with the 4th air inlet (13b), the 4th gas outlet (14b), the 4th water inlet (15b), the 5th delivery port (16b) and the 6th delivery port (17b), on the 3rd absorption tower (3c), be provided with the 5th air inlet (13c), the 5th gas outlet (14c), the 5th water inlet (15c), the 7th delivery port (16c) and the 8th delivery port (17c); Described the 3rd gas outlet (14a) joins with the 4th air inlet (13b), the 4th gas outlet (14b) joins with the 5th air inlet (13c), the 5th gas outlet (14c) joins with the 6th air inlet (18), the 4th water inlet (15b) and the 5th water inlet (15c) all join with the 9th delivery port (24), and the 5th delivery port (16b), the 6th delivery port (17b), the 7th delivery port (16c) and the 8th delivery port (17c) all join with the 6th water inlet (23).
3. according to the described a kind of ammoniacal liquor retracting device of claim 1, it is characterized in that: also be provided with the 7th gas outlet (20) between described second gas outlet (10) and the 3rd air inlet (13a), described escape pipe (19) is provided with the 7th air inlet (21), and described the 7th gas outlet (20) joins with the 7th air inlet (21).
4. according to the described a kind of ammoniacal liquor retracting device of claim 1, it is characterized in that: described adsorption tanks (4) are absorbent charcoal adsorption tank.
5. according to the described a kind of ammoniacal liquor retracting device of claim 1, it is characterized in that: described gas buffer jar (1) outer wall also is provided with two circle stiffening rings (25).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011101052033A CN102179134A (en) | 2011-04-26 | 2011-04-26 | Ammonia water recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011101052033A CN102179134A (en) | 2011-04-26 | 2011-04-26 | Ammonia water recovery device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102179134A true CN102179134A (en) | 2011-09-14 |
Family
ID=44565536
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011101052033A Pending CN102179134A (en) | 2011-04-26 | 2011-04-26 | Ammonia water recovery device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102179134A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102963909A (en) * | 2012-11-26 | 2013-03-13 | 苏州金宏气体股份有限公司 | Method for recovering and reutilizing waste ammonia gas in LED (light-emitting diode) manufacturing through ammonia water method |
| CN102963910A (en) * | 2012-11-26 | 2013-03-13 | 苏州金宏气体股份有限公司 | Method for recovering and reutilizing waste ammonia gas in LED (light-emitting diode) manufacturing through compression method |
| CN103933831A (en) * | 2014-04-22 | 2014-07-23 | 南通市海圣药业有限公司 | Method for recycling ammonia gas in process of producing 4-aminotrifluorotoluene |
| CN104056526A (en) * | 2014-07-02 | 2014-09-24 | 中国人民解放军第二炮兵装备研究院第六研究所 | Method and device for absorbing hydrazine class gas in confined space |
| CN107855003A (en) * | 2017-11-24 | 2018-03-30 | 江苏科技大学 | A kind of ammoniacal liquor recycling device of the ship denitrating system based on SCR |
| RU2754848C1 (en) * | 2020-12-09 | 2021-09-08 | Акционерное общество "Газпромнефть - Омский НПЗ" (АО "Газпромнефть-ОНПЗ") | Method for the regeneration of waste ammonia water and the extraction of mercaptans |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202087187U (en) * | 2011-04-26 | 2011-12-28 | 苏州利盛化工设备有限公司 | Ammonia water recovery device |
-
2011
- 2011-04-26 CN CN2011101052033A patent/CN102179134A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202087187U (en) * | 2011-04-26 | 2011-12-28 | 苏州利盛化工设备有限公司 | Ammonia water recovery device |
Non-Patent Citations (1)
| Title |
|---|
| 周启云: "磺胺生产中废气的治理和资源的回收利用", 《化工环保》 * |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102963909A (en) * | 2012-11-26 | 2013-03-13 | 苏州金宏气体股份有限公司 | Method for recovering and reutilizing waste ammonia gas in LED (light-emitting diode) manufacturing through ammonia water method |
| CN102963910A (en) * | 2012-11-26 | 2013-03-13 | 苏州金宏气体股份有限公司 | Method for recovering and reutilizing waste ammonia gas in LED (light-emitting diode) manufacturing through compression method |
| CN102963910B (en) * | 2012-11-26 | 2014-08-06 | 苏州金宏气体股份有限公司 | Method for recovering and reutilizing waste ammonia gas in LED (light-emitting diode) manufacturing through compression method |
| CN102963909B (en) * | 2012-11-26 | 2014-08-06 | 苏州金宏气体股份有限公司 | Method for recovering and reutilizing waste ammonia gas in LED (light-emitting diode) manufacturing through ammonia water method |
| CN103933831A (en) * | 2014-04-22 | 2014-07-23 | 南通市海圣药业有限公司 | Method for recycling ammonia gas in process of producing 4-aminotrifluorotoluene |
| CN103933831B (en) * | 2014-04-22 | 2015-12-09 | 南通市海圣药业有限公司 | A kind of recovery method producing ammonia in 4-5 amido benzotrifluoride technique |
| CN104056526A (en) * | 2014-07-02 | 2014-09-24 | 中国人民解放军第二炮兵装备研究院第六研究所 | Method and device for absorbing hydrazine class gas in confined space |
| CN104056526B (en) * | 2014-07-02 | 2016-04-13 | 中国人民解放军第二炮兵装备研究院第六研究所 | A kind of confined space hydrazine class GAS ABSORPTION method and device |
| CN107855003A (en) * | 2017-11-24 | 2018-03-30 | 江苏科技大学 | A kind of ammoniacal liquor recycling device of the ship denitrating system based on SCR |
| CN107855003B (en) * | 2017-11-24 | 2024-05-03 | 江苏科技大学 | Ammonia water recycling device of ship denitration system based on SCR |
| RU2754848C1 (en) * | 2020-12-09 | 2021-09-08 | Акционерное общество "Газпромнефть - Омский НПЗ" (АО "Газпромнефть-ОНПЗ") | Method for the regeneration of waste ammonia water and the extraction of mercaptans |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102179134A (en) | Ammonia water recovery device | |
| CN102068880B (en) | Method for recycling ammonia gas in industrial waste gas | |
| CN104028100A (en) | Absorption technology of oxynitride gas at normal pressure and apparatus | |
| CN210786860U (en) | Tail gas absorption device for recycling carbon dioxide | |
| CN103011084A (en) | Method for extracting iodine from dehydrate wet method diluted phosphoric acid reaction iodic waste gas | |
| CN103496777B (en) | Pretreatment method of ammonia-nitrogen wastewater | |
| CN102179135B (en) | Ammonia absorption device | |
| CN202087187U (en) | Ammonia water recovery device | |
| CN202087201U (en) | Ammonia absorption device | |
| CN104208987B (en) | Device for recovering tail gas in a kind of urea ammonium nitrate solution production | |
| CN201728055U (en) | Acid mist recovering and purifying equipment | |
| CN101830483A (en) | Production method for synthesizing ammonium bicarbonate fertilizer by using CO2 waste gas | |
| CN105344224B (en) | A kind of styrene waste gases processing method | |
| CN113457381A (en) | Energy-saving process for capturing and recovering carbon dioxide from chimney exhaust gas | |
| CN201990481U (en) | Concentration device for dilute hydrochloric acid | |
| CN107126826A (en) | Ammonia-contained tail gas treating device and method in prepared by a kind of soda ash | |
| CN203620498U (en) | Rare-earth waste gas treatment system | |
| CN202478634U (en) | Device for processing acid mist | |
| CN202844850U (en) | Offgas absorption device for anhydrous aluminum trichloride production | |
| CN103801173B (en) | The processing method of NOx waste gas in a kind of copper zinc catalyst preparation technology | |
| CN201333372Y (en) | Tail gas recovery device of methanol tower | |
| CN204656339U (en) | A kind of desulphurization denitration absorption reaction tower | |
| CN103570085A (en) | Device for treating high-concentration ammonia nitrogen in coking wastewater by using surfactant | |
| CN203235398U (en) | Waste ammonia gas absorbing system | |
| CN207024681U (en) | Novel acetone condensate recycling device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20110914 |