CN112107969B - An ammonia tail gas absorption tower and supporting energy recovery system - Google Patents
An ammonia tail gas absorption tower and supporting energy recovery system Download PDFInfo
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- CN112107969B CN112107969B CN202011108747.0A CN202011108747A CN112107969B CN 112107969 B CN112107969 B CN 112107969B CN 202011108747 A CN202011108747 A CN 202011108747A CN 112107969 B CN112107969 B CN 112107969B
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- outlet
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- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims abstract description 278
- 229910021529 ammonia Inorganic materials 0.000 title claims abstract description 142
- 238000011084 recovery Methods 0.000 title claims abstract description 114
- 238000010521 absorption reaction Methods 0.000 title claims abstract description 28
- 238000009835 boiling Methods 0.000 claims abstract description 131
- 238000005406 washing Methods 0.000 claims abstract description 107
- 239000007788 liquid Substances 0.000 claims abstract description 54
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 38
- 238000005201 scrubbing Methods 0.000 claims abstract description 16
- 238000005507 spraying Methods 0.000 claims description 17
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 6
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 6
- 230000005540 biological transmission Effects 0.000 claims description 6
- 239000007789 gas Substances 0.000 description 218
- 239000007921 spray Substances 0.000 description 13
- 239000006210 lotion Substances 0.000 description 9
- 230000000694 effects Effects 0.000 description 7
- 239000000945 filler Substances 0.000 description 4
- 230000008676 import Effects 0.000 description 3
- 239000000969 carrier Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000006096 absorbing agent Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/18—Absorbing units; Liquid distributors therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/1418—Recovery of products
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/40—Nitrogen compounds
- B01D2257/406—Ammonia
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
Abstract
本发明公开一种含氨气尾气吸收塔及配套能源回收系统，包括沸腾式氨尾气回收塔、洗气塔和回收组件，沸腾式氨尾气回收塔分别与洗气塔和回收组件相连通；沸腾式氨尾气回收塔具有第一尾气进口、第一尾气出口和第一洗液出口，洗气塔具有第二尾气进口、第二尾气出口和第二洗液出口，洗气塔能够与外部水源相连通，第一尾气出口与第二尾气进口相连通，第二洗液出口与沸腾式氨尾气回收塔相连通，沸腾式氨尾气回收塔内设置沸腾板，沸腾板具有进气口和出气口，进气口与出气口相连通，进气口朝向第一尾气进口方向设置，出气口朝向第二洗液出口与沸腾式氨尾气回收塔的连通处设置，第一尾气进口通过沸腾板与第一尾气出口相连通。
The invention discloses an ammonia-containing tail gas absorption tower and a matching energy recovery system, comprising a boiling ammonia tail gas recovery tower, a scrubbing tower and a recovery component, wherein the boiling ammonia tail gas recovery tower is respectively connected with the scrubbing tower and the recovery component; the boiling ammonia tail gas recovery tower has a first tail gas inlet, a first tail gas outlet and a first washing liquid outlet, the scrubbing tower has a second tail gas inlet, a second tail gas outlet and a second washing liquid outlet, the scrubbing tower can be connected with an external water source, the first tail gas outlet is connected with the second tail gas inlet, the second washing liquid outlet is connected with the boiling ammonia tail gas recovery tower, a boiling plate is arranged in the boiling ammonia tail gas recovery tower, the boiling plate has an air inlet and an air outlet, the air inlet is connected with the air outlet, the air inlet is arranged toward the first tail gas inlet, the air outlet is arranged toward the connection between the second washing liquid outlet and the boiling ammonia tail gas recovery tower, and the first tail gas inlet is connected with the first tail gas outlet through the boiling plate.
Description
Technical Field
The invention relates to the technical field of ammonia treatment equipment and peripheral supporting facilities thereof, in particular to an ammonia-containing tail gas absorption tower and a supporting energy recovery system.
Background
Ammonia is very soluble in water, and 1 volume of water can absorb 700 volumes of ammonia. Ammonia is a common raw material for industry, however, and is also a common tail gas pollution. The content of ammonia emission is regulated in the atmospheric emission standard, and the traditional technology has the principle of a gas washing tower, and the core of the traditional technology is that the ammonia absorption efficiency is increased by passing gas to be purified in the tower and then spraying water into the tower, spraying and atomizing, and simultaneously adding a filler and increasing the contact area of the gas and the water.
The traditional gas washing tower has the core working principle that water is sprayed into flowing gas, so that when the gas flows relatively at high speed, the mixed area of gas and water is relatively large, but due to the action of the relative force of water drops and air flowing, part of gas is not contacted with water all the time, the absorption space is large, the efficiency is low, and the traditional gas washing tower usually needs 3-4 stages of gas washing, so that the satisfactory emission condition can be achieved.
Therefore, how to change the current situation that the gas washing efficiency of the gas washing tower is low in the prior art becomes a problem to be solved urgently by those skilled in the art.
Disclosure of Invention
The invention aims to provide an ammonia-containing tail gas absorption tower and a matched energy recovery system, so as to solve the problems in the prior art and improve the treatment and recovery efficiency of ammonia-containing tail gas.
The ammonia-containing tail gas absorption tower comprises a boiling ammonia tail gas recovery tower, a gas washing tower and a recovery assembly, wherein the boiling ammonia tail gas recovery tower is respectively communicated with the gas washing tower and the recovery assembly, the boiling ammonia tail gas recovery tower is provided with a first tail gas inlet, a first tail gas outlet and a first washing liquid outlet, the gas washing tower is provided with a second tail gas inlet, a second tail gas outlet and a second washing liquid outlet, the gas washing tower can be communicated with an external water source, the first tail gas outlet is communicated with the second tail gas inlet, the second washing liquid outlet is communicated with the boiling ammonia tail gas recovery tower, a boiling plate is arranged in the boiling ammonia tail gas recovery tower, the gas inlet is communicated with the gas outlet, the gas inlet is arranged towards the direction of the first tail gas inlet, the gas outlet is arranged towards the position where the second tail gas outlet is communicated with the boiling ammonia tail gas recovery tower, and the first tail gas outlet is communicated with the first tail gas outlet through the boiling plate.
Preferably, the first tail gas inlet is located at the bottom of the boiling ammonia tail gas recovery tower, the first tail gas outlet is located at the top of the boiling ammonia tail gas recovery tower, the air inlet is located at the bottom of the boiling plate, the air outlet is located at the top of the boiling plate, the second washing liquid outlet is communicated with the top of the boiling plate, and the second washing liquid outlet can drain washing liquid discharged from the gas washing tower to the top of the boiling plate.
Preferably, the air inlet is arranged at one end of the boiling plate, which is close to the axis of the boiling ammonia tail gas recovery tower, the other end of the boiling plate is connected with the inner wall of the boiling ammonia tail gas recovery tower, and the boiling plate is gradually arranged in a downward inclination manner from one end connected with the boiling ammonia tail gas recovery tower towards the free end of the boiling plate.
Preferably, the number of the boiling plates is multiple, the multiple boiling plates are uniformly distributed along the axis of the boiling ammonia tail gas recovery tower, and the adjacent boiling plates are staggered.
Preferably, the number of the air outlets is multiple, the air outlets are uniformly distributed, and the diameter of the air inlet is larger than that of the air outlet.
Preferably, the free end of the boiling plate is connected with a washing liquor recovery pipe, the washing liquor recovery pipe is communicated with the first washing liquor outlet, the recovery assembly comprises a heat exchanger, the first washing liquor outlet is communicated with the heat exchanger, and the heat exchanger is connected with a concentrated ammonia water recovery element.
Preferably, the gas washing tower comprises a spraying area, a filling area and a collecting area which are sequentially communicated from top to bottom, the spraying area is provided with a spray head, the spray head is communicated with an external water source, a second tail gas outlet is formed in the top of the spraying area and is communicated with an external environment, a gas disperser is arranged in the collecting area, the first tail gas outlet is communicated with the collecting area by the gas disperser, and a second washing liquid outlet is formed in the collecting area.
Preferably, the number of the spray heads is multiple, the spray heads are uniformly distributed along the axis direction of the gas washing tower, the axis of the spray heads is perpendicular to the axis of the gas washing tower, and a plurality of spray heads of each group are uniformly distributed around the axis of the gas washing tower in a circumferential manner.
Preferably, a transmission pump body is arranged between the second washing liquid outlet and the boiling ammonia tail gas recovery tower.
Compared with the prior art, the ammonia-containing tail gas absorption tower and the matched energy recovery system have the following technical effects that the ammonia-containing tail gas absorption tower comprises a boiling ammonia tail gas recovery tower, a gas washing tower and a recovery assembly, wherein the boiling ammonia tail gas recovery tower is respectively communicated with the gas washing tower and the recovery assembly, the boiling ammonia tail gas recovery tower is provided with a first tail gas inlet, a first tail gas outlet and a first washing liquid outlet, the gas washing tower is provided with a second tail gas inlet, the second tail gas outlet and the second washing liquid outlet, the gas washing tower can be communicated with an external water source, the first tail gas outlet is communicated with the second tail gas inlet, the second washing liquid outlet is communicated with the boiling ammonia tail gas recovery tower, a boiling plate is arranged in the boiling plate and is provided with an air inlet and an air outlet, the air inlet is communicated with the air inlet is arranged towards the direction of the first tail gas inlet, the air outlet is arranged towards the communicating position of the second washing liquid outlet and the boiling ammonia tail gas recovery tower, and the first tail gas inlet is communicated with the first tail gas outlet through the boiling plate. When the ammonia-containing tail gas absorption tower and the matched energy recovery system are in operation, ammonia-containing tail gas enters the boiling ammonia tail gas recovery tower from the first tail gas inlet, the ammonia-containing tail gas enters the boiling plate from the air inlet, the surface of the boiling plate meets a water film absorbing a small amount of ammonia to form a boiling effect, a large amount of ammonia is absorbed, the low-ammonia tail gas treated by the boiling ammonia tail gas recovery tower enters the scrubbing tower from the first tail gas outlet, an external water source is introduced into the scrubbing tower and is contacted with the tail gas entering the scrubbing tower, ammonia in the ammonia is absorbed, purified qualified tail gas is discharged from the second tail gas outlet, dilute ammonia washing liquid concentrated in the scrubbing tower is introduced into the boiling ammonia tail gas recovery tower, a water film is formed on the boiling plate, ammonia in the ammonia-containing tail gas is circularly absorbed, hot concentrated ammonia washing liquid absorbing ammonia and heat enters the recovery assembly from the boiling ammonia tail gas recovery tower through the first washing liquid outlet, and ammonia and heat are recovered. In the prior art, the gas washing equipment adopts a mode of spraying washing liquid to tail gas, gas can be avoided by the washing liquid in the spraying process, the gas washing effect is poor, and the multistage gas washing equipment is required to be arranged, so that the gas washing working efficiency is reduced.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings that are needed in the embodiments will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and other drawings may be obtained according to these drawings without inventive effort for a person skilled in the art.
FIG. 1 is a schematic diagram of an ammonia-containing tail gas absorber and associated energy recovery system of the present invention;
Wherein, 1 is boiling formula ammonia tail gas recovery tower, 2 is the gas washing tower, 3 is the recovery unit, 4 is first tail gas import, 5 is first tail gas export, 6 is first lotion export, 7 is second tail gas import, 8 is second tail gas export, 9 is second lotion export, 10 is boiling plate, 11 is lotion recovery tube, 12 is heat exchanger, 13 is spray zone, 14 is the filler zone, 15 is the collecting zone, 16 is the shower nozzle, 17 is the gas disperser, 18 is the transmission pump body, 19 is strong ammonia water recovery element, 20 is external water source.
Detailed Description
The following description of the embodiments of the present invention will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present invention, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
The invention aims to provide an ammonia-containing tail gas absorption tower and a matched energy recovery system, so as to solve the problems in the prior art and improve the treatment and recovery efficiency of ammonia-containing tail gas.
In order that the above-recited objects, features and advantages of the present invention will become more readily apparent, a more particular description of the invention will be rendered by reference to the appended drawings and appended detailed description.
Referring to fig. 1, fig. 1 is a schematic diagram of an ammonia-containing tail gas absorption tower and a matched energy recovery system according to the present invention.
The invention provides an ammonia-containing tail gas absorption tower and a matched energy recovery system, which comprise a boiling ammonia tail gas recovery tower 1, a gas washing tower 2 and a recovery component 3, wherein the boiling ammonia tail gas recovery tower 1 is respectively communicated with the gas washing tower 2 and the recovery component 3, the boiling ammonia tail gas recovery tower 1 is provided with a first tail gas inlet 4, a first tail gas outlet 5 and a first washing liquid outlet 6, the gas washing tower 2 is provided with a second tail gas inlet 7, a second tail gas outlet 8 and a second washing liquid outlet 9, the gas washing tower 2 can be communicated with an external water source 20, the first tail gas outlet 5 is communicated with the second tail gas inlet 7, the second washing liquid outlet 9 is communicated with the boiling ammonia tail gas recovery tower 1, a boiling plate 10 is arranged in the boiling ammonia tail gas recovery tower 1, the boiling plate 10 is provided with a gas inlet and a gas outlet, the gas inlet is arranged towards the direction of the first tail gas inlet 4, the gas outlet is arranged towards the position where the second washing liquid outlet 9 is communicated with the boiling ammonia tail gas recovery tower 1, and the first tail gas inlet 4 is communicated with the first outlet 5 through the boiling plate 10.
When the ammonia-containing tail gas absorption tower and the matched energy recovery system are in operation, ammonia-containing tail gas enters the boiling type ammonia tail gas recovery tower 1 through the first tail gas inlet 4, the ammonia-containing tail gas enters the boiling plate 10 through the air inlet, the surface of the boiling plate 10 is contacted with a water film absorbing a small amount of ammonia to form a boiling effect, a large amount of ammonia is absorbed, the low-ammonia tail gas treated by the boiling type ammonia tail gas recovery tower 1 enters the scrubbing tower 2 through the first tail gas outlet 5, an external water source 20 is introduced into the scrubbing tower 2 and is contacted with the tail gas entering the scrubbing tower 2, ammonia in the absorption of the ammonia is discharged through the second tail gas outlet 8, dilute ammonia washing liquid concentrated in the scrubbing tower 2 is introduced into the boiling type ammonia tail gas recovery tower 1, a water film is formed on the boiling plate 10, the ammonia in the ammonia-containing tail gas is circularly absorbed, the hot concentrated ammonia washing liquid absorbing ammonia and heat is introduced into the recovery assembly 3 through the first outlet 6, and ammonia and heat are recovered. In the prior art, the gas washing equipment adopts a mode of spraying washing liquid to tail gas, gas can be avoided by the washing liquid in the spraying process, the gas washing effect is poor, and the multistage gas washing equipment is required to be arranged, so that the gas washing working efficiency is reduced.
Wherein, first tail gas import 4 is located the bottom of boiling ammonia tail gas recovery tower 1, first tail gas export 5 is located the top of boiling ammonia tail gas recovery tower 1, the air inlet is located the bottom of boiling board 10, make things convenient for the ammonia gas tail gas to get into in the boiling board 10, second lotion export 9 is linked together with the top of boiling board 10, second lotion export 9 can be with the top of gas washing tower 2 exhaust lotion drainage to boiling board 10, the gas outlet is located the top of boiling board 10, the ammonia gas tail gas gets into in the water film at boiling board 10 top by the gas outlet, accomplish the gas washing, the phenomenon that the lotion "avoided" tail gas takes place.
Wherein, the air inlet sets up in the one end that boiling plate 10 is close to the axis of boiling ammonia tail gas recovery tower 1, and the other end of boiling plate 10 links to each other with the inner wall of boiling ammonia tail gas recovery tower 1, and boiling plate 10 is from the one end that links to each other with boiling ammonia tail gas recovery tower 1 towards the free end of boiling plate 10 slope setting gradually downwards, and the ammonia that conveniently gets into in the boiling plate 10 in the boiling ammonia tail gas recovery tower 1, and the water film at the boiling plate 10 top of being convenient for simultaneously flows into first lotion export 6 smoothly after absorbing ammonia.
In this embodiment, the quantity of boiling board 10 is the polylith to further improve boiling formula ammonia tail gas recovery tower 1's work efficiency, polylith boiling board 10 set up along boiling formula ammonia tail gas recovery tower 1's axis equipartition, improve ammonia treatment uniformity, in addition, improved boiling formula ammonia tail gas recovery tower 1's structural stability, adjacent boiling board 10 staggered arrangement of row strengthen ammonia treatment effect.
More specifically, the quantity of gas outlet is a plurality of, and a plurality of gas outlets equipartition sets up, has improved the degree of consistency in the water film that ammonia gas tail gas got into the lotion and formed, strengthens ammonia treatment effeciency, and in this embodiment, the diameter of air inlet is bigger than the diameter of gas outlet, ensures that ammonia gas tail gas gets into boiling plate 10 smoothly, and then gets into in the water film and wash gas.
In order to collect the concentrated hot ammonia washing liquid conveniently, the free end of the boiling plate 10 is connected with a washing liquid recovery pipe 11, the washing liquid recovery pipe 11 is communicated with the first washing liquid outlet 6, the recovery assembly 3 comprises a heat exchanger 12, the first washing liquid outlet 6 is communicated with the heat exchanger 12, the collected concentrated hot ammonia washing liquid exchanges heat with water or other heat carriers in the heat exchanger 12 for heating or other purposes in a factory, and the heat exchanger 12 is connected with a concentrated ammonia water recovery element 19 for waiting for cyclic production.
Further, the gas washing tower 2 comprises a spraying area 13, a filling area 14 and a collecting area 15 which are sequentially communicated from top to bottom, the spraying area 13 is provided with a spray head 16, the spray head 16 is communicated with an external water source 20, a second tail gas outlet 8 is formed in the top of the spraying area 13, the second tail gas outlet 8 is communicated with the external environment, the collecting area 15 is provided with a gas disperser 17, the first tail gas outlet 5 is communicated with the collecting area 15 by the gas disperser 17, and the second washing liquid outlet 9 is formed in the collecting area 15. The low-ammonia tail gas led out from the first tail gas outlet 5 enters the gas washing tower 2 through the second tail gas inlet 7, is uniformly dispersed into the gas washing tower 2 through the gas disperser 17, is guided to move to the upper part of the gas washing tower 2 by air pressure, clean water is pressurized and sprayed out from a nozzle at the top of the gas washing tower 2, a fog rain area is formed in the spraying area 13, water falls into the filling area 14 downwards, a water film is formed in the filling area 14, contacts with the low-ammonia tail gas from the collecting area 15, absorbs ammonia in the low-ammonia tail gas, the purified and qualified tail gas is discharged from the second tail gas outlet 8, and the unqualified gas is pressurized again and enters the gas washing process again.
In order to form uniform fog rain in the spraying area 13, the number of the spray heads 16 is multiple, the spray heads 16 of multiple groups are uniformly distributed along the axial direction of the gas washing tower 2, the axial line of the spray heads 16 is perpendicular to the axial line of the gas washing tower 2, and a plurality of spray heads 16 of each group are uniformly distributed around the axial line of the gas washing tower 2.
In addition, a transmission pump body 18 is arranged between the second washing liquid outlet 9 and the boiling ammonia tail gas recovery tower 1 to ensure smooth transmission of washing liquid, and similarly, the transmission pump body 18 is arranged between the first washing liquid outlet 6 and the heat exchanger 12, and between the external water source 20 and the gas washing tower 2 to ensure normal operation of the system.
When the ammonia-containing tail gas absorption tower and the matched energy recovery system are in operation, the ammonia-containing tail gas is pressurized from a pipeline at the lower part of the boiling ammonia tail gas recovery tower 1 to enter the boiling plate 10, meets a water film absorbing a small amount of ammonia on the surface of the boiling plate 10 to form a boiling effect, finishes the absorption of a large amount of ammonia gas, and outputs the low-ammonia tail gas subjected to primary absorption from a pipeline at the top of the boiling ammonia tail gas recovery tower 1; the low ammonia tail gas enters the lower part of the gas washing tower 2 through a bent pipe, is uniformly dispersed into the tower through a gas disperser 17, is guided to move to the upper part of the gas washing tower 2 by air pressure, the clean water is pressurized and sprayed out from a nozzle at the top of the gas washing tower 2, a fog rain area is formed in the top area, water falls down into a filler area 14, forms a water film on the filler, contacts with the low ammonia tail gas from the tower downwards, absorbs ammonia in the low ammonia tail gas, the purified and qualified tail gas is discharged from the top of the tower through a detector and a buffer, the reject gas is pressurized again from the buffer, and enters the gas washing process again, the concentrated dilute ammonia washing liquid at the lower part of the gas washing tower 2 is pumped into an absorption water film formed on a boiling plate 10 through a pump, so that heat and ammonia gas in the high ammonia tail gas are absorbed, the hot dense ammonia liquid after the ammonia and the heat are discharged from the tower is discharged from the bottom of the tower, a large amount of waste heat is exchanged with water or other heat carriers through a heat preservation pipeline to be produced for preheating materials or be sent to a production office area, the dense ammonia water is recycled 19 to be used for heat recovery in a factory area, and the dense ammonia water is recycled for heating element for waiting.
The principles and embodiments of the present invention have been described in detail with reference to specific examples, which are provided herein to facilitate understanding of the principles and embodiments of the present invention and to provide further advantages and practical applications for those of ordinary skill in the art in light of the present teachings. In view of the foregoing, this description should not be construed as limiting the invention.
Claims (8)
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| CN202011108747.0A CN112107969B (en) | 2020-10-16 | 2020-10-16 | An ammonia tail gas absorption tower and supporting energy recovery system |
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| CN202011108747.0A CN112107969B (en) | 2020-10-16 | 2020-10-16 | An ammonia tail gas absorption tower and supporting energy recovery system |
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| CN206549409U (en) * | 2017-02-14 | 2017-10-13 | 青岛长荣化工科技有限公司 | Treatment device for ammonia-containing waste gas |
| CN213853813U (en) * | 2020-10-16 | 2021-08-03 | 吉林市吉化江城油脂化工有限责任公司 | Ammonia-containing tail gas absorption tower and supporting energy recovery system |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN101105348A (en) * | 2006-11-04 | 2008-01-16 | 青岛大学 | Ammonia-water absorption car air conditioner |
| CN102120137B (en) * | 2011-02-16 | 2012-12-26 | 安徽淮化股份有限公司 | System and process for capturing and absorbing sulfur dioxide and carbon dioxide at normal pressure by using ammonia method |
| CN103894048B (en) * | 2014-04-18 | 2015-12-09 | 中石化南京工程有限公司 | A kind of method processing low concentration ammonia-containing exhaust |
| CN106823692A (en) * | 2017-03-22 | 2017-06-13 | 天华化工机械及自动化研究设计院有限公司 | A kind of ammonia-contaminated gas zero-emission and ammonia reclaiming process |
| CN108722163B (en) * | 2017-09-07 | 2019-06-07 | 江苏新世纪江南环保股份有限公司 | A kind of method of ammonia desulfurization control aerosol generation in absorption process |
| CN108722132A (en) * | 2017-11-24 | 2018-11-02 | 羿太环保科技（上海）有限公司 | A kind of falling film type absorption condensation device and method |
| CN207871823U (en) * | 2018-01-04 | 2018-09-18 | 徐州鑫宇光伏科技有限公司 | A kind of plated film exhaust gas depositing dust absorption plant that solar battery sheet production technology uses |
| CN108970341A (en) * | 2018-10-15 | 2018-12-11 | 广东宏昊化工有限公司 | A kind of exhaust treatment system recycling high concentration ammonium hydroxide from ammonia-containing exhaust |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN206549409U (en) * | 2017-02-14 | 2017-10-13 | 青岛长荣化工科技有限公司 | Treatment device for ammonia-containing waste gas |
| CN213853813U (en) * | 2020-10-16 | 2021-08-03 | 吉林市吉化江城油脂化工有限责任公司 | Ammonia-containing tail gas absorption tower and supporting energy recovery system |
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