CN202590610U - Desulphurization device through circulating absorption of liquid ammonia - Google Patents
Desulphurization device through circulating absorption of liquid ammonia Download PDFInfo
- Publication number
- CN202590610U CN202590610U CN 201220190681 CN201220190681U CN202590610U CN 202590610 U CN202590610 U CN 202590610U CN 201220190681 CN201220190681 CN 201220190681 CN 201220190681 U CN201220190681 U CN 201220190681U CN 202590610 U CN202590610 U CN 202590610U
- Authority
- CN
- China
- Prior art keywords
- desulfurizing tower
- absorption liquid
- kerve
- circulating
- absorption
- 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 - Lifetime
Links
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims abstract description 34
- 238000010521 absorption reaction Methods 0.000 title claims abstract description 25
- 239000007788 liquid Substances 0.000 claims abstract description 19
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 238000005406 washing Methods 0.000 claims abstract description 11
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 18
- 239000003546 flue gas Substances 0.000 claims description 18
- 230000003009 desulfurizing effect Effects 0.000 claims description 17
- 238000006477 desulfuration reaction Methods 0.000 claims description 12
- 230000008676 import Effects 0.000 claims description 5
- 239000012530 fluid Substances 0.000 claims description 3
- 239000007921 spray Substances 0.000 abstract description 5
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 abstract description 4
- 239000000779 smoke Substances 0.000 abstract description 3
- 238000004140 cleaning Methods 0.000 abstract 2
- 239000006227 byproduct Substances 0.000 abstract 1
- 238000005192 partition Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 6
- 239000007789 gas Substances 0.000 description 5
- 239000002002 slurry Substances 0.000 description 4
- AOSFMYBATFLTAQ-UHFFFAOYSA-N 1-amino-3-(benzimidazol-1-yl)propan-2-ol Chemical compound C1=CC=C2N(CC(O)CN)C=NC2=C1 AOSFMYBATFLTAQ-UHFFFAOYSA-N 0.000 description 2
- PQUCIEFHOVEZAU-UHFFFAOYSA-N Diammonium sulfite Chemical compound [NH4+].[NH4+].[O-]S([O-])=O PQUCIEFHOVEZAU-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 230000023556 desulfurization Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 238000004176 ammonification Methods 0.000 description 1
- ZETCGWYACBNPIH-UHFFFAOYSA-N azane;sulfurous acid Chemical compound N.OS(O)=O ZETCGWYACBNPIH-UHFFFAOYSA-N 0.000 description 1
- 230000005465 channeling Effects 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
Images
Landscapes
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
Abstract
The utility model discloses a desulphurization device through circulating absorption of liquid ammonia. The device comprises a desulfurizer (1) provided with an air inlet (2) at the lower portion and an air outlet (3) at the top. The desulfurizer (1) further comprises a washing unit, a wire mesh demister (12), a spray nozzle (5), a plurality of cleaning chambers (7) and a bottom groove (8) from bottom to top, wherein a base plate (6) of each cleaning chamber (7) is provided with a plurality of holes for smoke and absorption liquid to pass through; and the washing unit comprises a water inlet (14), the spray nozzle (5), a vent cap (10), a partition (11) and a water outlet (13). According to the desulphurization device, the structure is simple, the problems of short contact time and insufficient contact of the smoke with the absorption liquid are solved, by-products generated through ammonia processing on sulfur dioxide can be recycled, the occupied space is small, and the cost for equipment investment and operation is reduced greatly.
Description
Technical field
The utility model relates to a kind of circulating absorption solution ammonia desulfuration equipment, and being specifically related to ammonia is raw material reclaims oxysulfide from flue gas desulfurizer.
Background technology
The ammonia process of desulfurization is to utilize ammonia spirit to absorb the SO in the flue gas
2Produce ammonium bisulfite and sulfurous acid ammonia, and ammonium sulfite is also to SO
2Very strong absorbability is arranged, and the two all is the main absorber in the ammonia process, and ammonium bisulfite also can produce ammonium sulfite through ammonification.At present, the spray column that wet ammonia process desulfurizing technology adopted is counted the lower main cause of efficient has two.The one, because exhaust gas volumn is very big, the diameter of required desulfurizing tower is very big, and the height of desulfurizing tower is generally lower, has channeling easily, makes flue gas flow field inhomogeneous, Gu cause gas-liquid-three-phase contact area to reduce.The 2nd, the drop that spraying layer sprayed is bigger, and the mass transfer specific area is less, and mass tranfer coefficient is also little, causes gas-liquid mass-transfer efficiency to reduce.Can increase liquid-gas ratio though strengthen the circulation of desulfurizer slurry, operating cost will significantly increase again.Particularly, when needs higher to concentration ratio, the SO that throughput is bigger
2Gas (gas that for example has rich sulfur mineral burning to produce) when absorbing, the time period that flue gas contacts with absorption liquid, absorbs insufficient.
The utility model content
To above not enough the utility model a kind of circulating absorption solution ammonia process of desulfurization tower is provided, it is short mainly to solve flue gas and absorption liquid time of contact, contacts the problem that has the escaping of ammonia in insufficient, the flue gas.
The technical scheme that the utility model adopts is: a kind of circulating absorption solution ammonia desulfuration equipment, comprise desulfurizing tower, and the desulfurizing tower bottom is provided with air inlet; Exhaust outlet is arranged on the top of tower; In tower, be followed successively by washing equipment, wire mesh demister, shower nozzle, several clean rooms and kerve from bottom to top; The base plate of clean room is provided with some holes that flue gas and absorption liquid are passed through; Kerve is provided with valve, through circulating pump the circulation fluid in the kerve is transported to the absorption liquid import; Said washing equipment comprises water inlet, shower nozzle, abat-vent and delivery port, through circulating pump the water that flows out in the delivery port is transported in the water inlet.The quantity of said clean room is 3～6 layers.
Compare with traditional wet ammonia method for flue gas desulfurizing device; The utlity model has following advantage: in the clean room, form continuously and fierce flue gas turbulent flow; Greatly optimized the flue gas flow field in the desulfurizing tower; Gas-liquid mass transfer in the reinforcing desulfuration tower between flue gas and the desulfurizer slurry, and then improve desulfuration efficiency.This device forces flue gas that turbulent flow takes place on the one hand; Dead angle on the other hand removes smoke; Make flue gas in desulfurizing tower, both realize even flow field optimization by different level; Continually strengthen the mass transfer between flue gas and the desulfurizer slurry again, effectively prevented of the influence of desulfurizer slurry spray blind area, desulfurizing tower edge, thereby made gas-liquid mass transfer efficient can improve 25～35% desulfuration efficiency.In addition, the utility model also is provided with washing equipment and silk screen foam removal equipment, has reduced the escape of sulfur dioxide and ammonia, and desulfuration efficiency increases greatly; This plant area area is little, greatly reduced investment of devices and operating cost.
Description of drawings
Fig. 1 is the structural representation of the utility model.
Wherein: the 1-desulfurizing tower; The 2-air inlet; The 3-exhaust outlet; The import of 4-absorption liquid; The 5-shower nozzle; The 6-base plate; The 7-clean room; The 8-kerve; The 9-valve, 10-abat-vent, 11-division board, 12-wire mesh demister, 13-discharge outlet, 14-water inlet, 15-circulating pump.
The specific embodiment
Below in conjunction with the accompanying drawing and the specific embodiment the utility model is done explanation in further detail.
With reference to Fig. 1, a kind of circulating absorption solution ammonia desulfuration equipment comprises desulfurizing tower 1, and desulfurizing tower 1 bottom is provided with air inlet 2; Exhaust outlet 3 is arranged on the top of desulfurizing tower 1; In desulfurizing tower 1, be followed successively by washing equipment, wire mesh demister 12, shower nozzle 5, four layers of clean room 7 and kerve 8 from bottom to top; The base plate 6 of clean room 7 is provided with some holes that flue gas and absorption liquid are passed through; Kerve 8 is provided with valve 9, through circulating pump 15 circulation fluid in the kerve 9 is transported to absorption liquid import 4; Said washing equipment comprises water inlet 14, shower nozzle 5, abat-vent 10, division board 11, delivery port 13, through circulating pump 15 water that flows out in the delivery port 13 is transported in the water inlet 14.
The utility model adopts flue gas and the reverse method that contacts of absorbent, reacts fully thoroughly.Flue gas gets in the tower from air inlet 1, midway will be 7 react with absorption liquid through the clean room, cigarette at last through wire mesh demister 12 foam removals, washing equipment washing after exhaust outlet 8 rows to atmosphere, product falls into kerve.Absorption liquid also constantly injects the absorption liquid import by circulating pump, sprays through shower nozzle.Absorption liquid is with after rich sulphur gas contacts, and the concentration of reaction product continues to increase.When the concentration of absorption liquid acquires a certain degree, discharge through valve, can recycle.
Though the utility model with preferred embodiment openly as above; But they are not to be used for limiting the utility model; Anyly be familiar with this art; In spirit that does not break away from the utility model and scope, certainly when can doing various variations, so being as the criterion of should being defined with the application's claim protection domain of the protection domain of the utility model.
Claims (2)
1. a circulating absorption solution ammonia desulfuration equipment comprises desulfurizing tower (1), and desulfurizing tower (1) bottom is provided with air inlet (2); Exhaust outlet (3) is arranged on the top of desulfurizing tower (1); It is characterized in that: in desulfurizing tower (1), comprise washing equipment, wire mesh demister (12), shower nozzle (5), several layers clean room (7) and kerve (8) from bottom to top successively; The base plate (6) of clean room (7) is provided with some holes that flue gas and absorption liquid are passed through; Kerve (8) is provided with valve (9), through circulating pump (15) circulation fluid in the kerve (9) is transported to absorption liquid import (4); Said washing equipment comprises water inlet (14), shower nozzle (5), abat-vent (10), division board (11), delivery port (13), through circulating pump (15) water that flows out in the delivery port (13) is transported in the water inlet (14).
2. a kind of circulating absorption solution ammonia desulfuration equipment as claimed in claim 1 is characterized in that: the quantity of said clean room is 3～6 layers.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220190681 CN202590610U (en) | 2012-05-02 | 2012-05-02 | Desulphurization device through circulating absorption of liquid ammonia |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220190681 CN202590610U (en) | 2012-05-02 | 2012-05-02 | Desulphurization device through circulating absorption of liquid ammonia |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202590610U true CN202590610U (en) | 2012-12-12 |
Family
ID=47308192
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220190681 Expired - Lifetime CN202590610U (en) | 2012-05-02 | 2012-05-02 | Desulphurization device through circulating absorption of liquid ammonia |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202590610U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111450622A (en) * | 2020-04-24 | 2020-07-28 | 大唐环境产业集团股份有限公司 | Demister flushing system capable of automatically adjusting water balance of desulfurization tower and control method |
| CN112439219A (en) * | 2019-09-05 | 2021-03-05 | 中石油吉林化工工程有限公司 | Four-effect evaporator for preparing acrylonitrile |
| CN113426276A (en) * | 2021-07-01 | 2021-09-24 | 江苏新世纪江南环保股份有限公司 | Ammonia desulphurization energy-saving device |
-
2012
- 2012-05-02 CN CN 201220190681 patent/CN202590610U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112439219A (en) * | 2019-09-05 | 2021-03-05 | 中石油吉林化工工程有限公司 | Four-effect evaporator for preparing acrylonitrile |
| CN111450622A (en) * | 2020-04-24 | 2020-07-28 | 大唐环境产业集团股份有限公司 | Demister flushing system capable of automatically adjusting water balance of desulfurization tower and control method |
| CN111450622B (en) * | 2020-04-24 | 2024-02-09 | 大唐环境产业集团股份有限公司 | Demister flushing system capable of automatically adjusting water balance of desulfurizing tower and control method |
| CN113426276A (en) * | 2021-07-01 | 2021-09-24 | 江苏新世纪江南环保股份有限公司 | Ammonia desulphurization energy-saving device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201380037Y (en) | Flue-gas cleaner with functions of desulphurization, denitration, concentration and crystal | |
| CN203355586U (en) | Multi-stage-absorption ammonia desulphurization system | |
| CN202725003U (en) | Compound type multifunctional ammonia desulphurization device | |
| CN201880482U (en) | Stepped spray tower for desulfurization by ammonia method | |
| CN105597513A (en) | Flue gas desulfurizing and dust removing device of coal-fired boiler | |
| CN201208544Y (en) | Desulfuration absorbing tower with dual-tower structure | |
| CN101422693A (en) | Sulphuric acid tail-gas deep desulfurization method | |
| CN101890281A (en) | Forward flow and backward flow combined spray desulfurizing tower | |
| US11534717B2 (en) | Ammonia desulphurization and oxidation apparatus and method | |
| CN202590610U (en) | Desulphurization device through circulating absorption of liquid ammonia | |
| CN204637975U (en) | Flue gas desulfurization enhancing device | |
| CN204996307U (en) | Ozone oxidation and ammonia process of industry flue gas spray joint SOx/NOx control device | |
| CN201189447Y (en) | Flue gas desulfurization absorption tower | |
| CN201669053U (en) | Desulfurizing device with gas fume washing component | |
| CN108434949A (en) | A kind of the low energy consumption wet desulfurizing process and device of zonal control | |
| CN104941411A (en) | Ozone oxidation and ammonia spraying combined desulfuration and denitration method and device for industrial smoke | |
| CN202590600U (en) | Desulfurization device for preparing ammonium bisulfite solution through ammonia process | |
| CN208287776U (en) | A kind of flue gas desulphurization system | |
| CN202590611U (en) | Circulating absorption liquid ammonia desulphurization tower | |
| CN102553430A (en) | Bicyclic high-efficiency desulfurization absorption tower and desulfurization system employing tower | |
| CN207899255U (en) | A kind of desulphurization plant | |
| CN202590601U (en) | Production device for ammonium bisulfate solution | |
| CN202270475U (en) | Wet type spraying, desulfuration and denitration integrated device | |
| CN107519749A (en) | A kind of ammonia ore deposit mixes sulfur removal technology technology | |
| CN212819076U (en) | System for flue gas pollutant degree of depth desorption |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Desulphurization device through circulating absorption of liquid ammonia Effective date of registration: 20180529 Granted publication date: 20121212 Pledgee: Gaotang Tsing long village bank Limited by Share Ltd Pledgor: Shandong Tiantai Steel Plastic Co., Ltd. Registration number: 2018370000098 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20180620 Granted publication date: 20121212 Pledgee: Gaotang Tsing long village bank Limited by Share Ltd Pledgor: Shandong Tiantai Steel Plastic Co., Ltd. Registration number: 2018370000098 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Desulphurization device through circulating absorption of liquid ammonia Effective date of registration: 20180702 Granted publication date: 20121212 Pledgee: Gaotang Tsing long village bank Limited by Share Ltd Pledgor: Shandong Tiantai Steel Plastic Co., Ltd. Registration number: 2018370000120 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20190530 Granted publication date: 20121212 Pledgee: Gaotang Tsing long village bank Limited by Share Ltd Pledgor: Shandong Tiantai Steel Plastic Co., Ltd. Registration number: 2018370000120 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190705 Address after: 457199 Grace Town 17 -108, Yumin Road and FutureRoad Intersection, Puyang County, Henan Province Patentee after: Henan Muhua Chemical Co., Ltd. Address before: 252800 Shandong Tiantai Steel Plastic Co., Ltd. Liaocheng Gaotang County, Shandong Province, Luzhuang Village, Jiangdian Township Patentee before: Shandong Tiantai Steel Plastic Co., Ltd. |
|
| TR01 | Transfer of patent right | ||
| CX01 | Expiry of patent term |
Granted publication date: 20121212 |
|
| CX01 | Expiry of patent term |