CN103599686A - Chemical waste gas treatment equipment - Google Patents
Chemical waste gas treatment equipment Download PDFInfo
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- CN103599686A CN103599686A CN201310617451.5A CN201310617451A CN103599686A CN 103599686 A CN103599686 A CN 103599686A CN 201310617451 A CN201310617451 A CN 201310617451A CN 103599686 A CN103599686 A CN 103599686A
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Abstract
The invention relates to chemical waste gas treatment equipment which comprises a first water tank, a second water tank and a chemical treatment tank, wherein a first outlet of the first water tank is connected with a chemical treatment inlet of the chemical treatment tank; a chemical treatment outlet of the chemical treatment tank is connected with a second inlet of the second water tank; a second outlet of the second water tank is communicated with a gas inlet of a waste gas treatment tower; a spraying layer, a dehydration layer and an activated carbon layer are sequentially arranged inside the waste gas treatment tower; a first inlet, the chemical treatment inlet and a second inlet of the first water tank are all extended to the positions under the liquid level; partitioning plates are arranged inside the first water tank, the second water tank and the chemical treatment tank; the partitioning plates are positioned under the liquid level; small holes are formed in the partitioning plates; the first inlet, the chemical treatment inlet and the second inlet are all inserted to the positions below the partitioning plates. By adopting the partitioning plates with the small holes, large bubbles can be cut into small bubbles, so that a gas can be sufficiently reacted and absorbed inside a liquid, and moreover the bubbles can be distributed in a large area without stirring, so that the equipment is beneficial to absorption of harmful gases by the liquid.
Description
Technical field
The present invention relates to chemical emission process field, especially relate to a kind of chemical emission treatment facility.
Background technology
Chemical emission refers to the poisonous and hazardous gas of being discharged by chemical plant in Chemical Manufacture.It is a lot of that chemical emission often contains pollutant kind, and physics and chemistry character is complicated, and toxicity is also not quite similar, serious environment pollution and affect health.The chemical emission composition difference that different Chemical Manufacture industries produce is very large.As mainly contained chlorine, hydrogen chloride, vinyl chloride, mercury, acetylene etc. in the waste gas of chlor-alkali industry generation, in the waste gas that Nitrogenous Fertilizer Industry produces, mainly contain nitrogen oxide, carbamide dust, carbon monoxide, ammonia, sulfur dioxide, methane etc.At present, at waste gas treatment equipment, be all air inlet pipe to be directly passed into liquid level with the harmful substance in lower absorption waste gas, the gas passing into due to flue gas leading normally enters with bubble form, the pernicious gas of bubble surface could be by liquid absorption, the pernicious gas of bubble inside is not absorbed direct discharge, and waste gas only reacts with flue gas leading liquid around, flue gas leading liquid absorption pernicious gas is around saturated no longer to be absorbed, the object that absorbs pernicious gas will do not reached like this, at present, the measure adopting adds agitating device exactly, make liquid flow, guarantee that flue gas leading has enough reaction liquids around, yet this mode not only needs to waste electric power, and can make the gas being dissolved in liquid again separate out, do not reach the object that absorbs pernicious gas yet.
Summary of the invention
Technical problem to be solved by this invention is to provide and does not a kind ofly need agitating device and can guarantee the chemical emission treatment facility that pernicious gas fully absorbs.
The present invention solves the technical scheme that its technical problem takes: a kind of chemical emission treatment facility, comprise the first airtight water tank, the second water tank and chemical processing tank, the first outlet of the first water tank is connected with the chemical treatment import of chemical processing tank, the chemical treatment outlet of chemical processing tank is connected with the second import of the second water tank, the second outlet of the second water tank is communicated with the air inlet of exhaust gas treating tower, exhaust gas treating tower inside is provided with spraying layer successively, dehydration layer and active carbon layer, the first import of the first described water tank, chemical treatment import and the second import all extend into below liquid level, the first described water tank, in the second water tank and chemical processing tank, be provided with a dividing plate, dividing plate is positioned at below liquid level, described dividing plate is provided with the aperture for bubble is cut apart of array arrangement, described the first import, chemical treatment import and the second import are all inserted below dividing plate.
Further, in order to guarantee waste gas form reactive absorption with minute bubbles in liquid, the first described import, chemical treatment import and the second import department are provided with cellular gas outlet.
Further, for the EGT of the first import department is reduced, the first described import department is provided with a heat exchanger.
Further, in order to make the water under spray state recycle, described exhaust-gas treatment tower bottom is provided with storage tank, and the delivery port of storage tank connects filtration system, by water pump, is connected with the shower in spraying layer.
Further, for the content of the waste gas oxynitrides that can guarantee to discharge reduces, between described dehydration layer and active carbon layer, be provided with SCR catalytic unit.
Further, in order to reduce the speed of waste gas in entering exhaust gas treating tower, described exhaust gas treating tower is cylindric, and its air inlet is opened in the tangential direction of exhaust gas treating tower cylinder.
The invention has the beneficial effects as follows: after having adopted said structure, by being with foraminate dividing plate air pocket can be divided into minute bubbles, carry out reactive absorption, make gas at the enough abundant reactive absorption of internal energy of liquid, and do not need to stir and bubble larger area can be distributed; Use cellular gas outlet when gas enters liquid, first to cut apart, cutting apart afterwards by dividing plate, what bubble can be cut apart is less, is more conducive to liquid absorption pernicious gas.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
In figure: 1, the first import; 2, dividing plate; 3, cellular gas outlet; 4, the first outlet; 5, the first water tank; 6, chemical treatment import; 7, chemical processing tank; 8, chemical treatment outlet; 9, the second water tank; 10, the second import; 11, the second outlet; 12, spraying layer; 13, air inlet; 14, storage tank; 15, filtration system; 16, water pump; 17, shower; 18, dehydration layer; 19, SCR catalytic unit; 20, active carbon layer.
The specific embodiment
Below in conjunction with accompanying drawing, the present invention is described in detail.
A kind of chemical emission treatment facility as shown in Figure 1, comprise the first airtight water tank 5, the second water tank 9 and chemical processing tank 7, the first outlet 1 of the first water tank 5 is connected with the chemical treatment import 6 of chemical processing tank 7, the chemical treatment outlet 8 of chemical processing tank 7 is connected with the second import 10 of the second water tank 9, the second outlet 11 of the second water tank 9 is communicated with the air inlet 13 of exhaust gas treating tower, exhaust gas treating tower inside is provided with spraying layer 12 successively, dehydration layer 18 and active carbon layer 20, the first import 1 of the first described water tank 5, chemical treatment import 6 and the second import 10 all extend into below liquid level, the first described water tank 5, in the second water tank 9 and chemical processing tank 7, be provided with a dividing plate 2, dividing plate 2 is positioned at below liquid level, described dividing plate 2 is provided with the aperture for bubble is cut apart of array arrangement, described the first import 1, chemical treatment import 6 and the second import 10 are all inserted dividing plate below 2, the first described import 1, chemical treatment import 6 and the second import 10 places are provided with cellular gas outlet 3.
Because waste gas out from equipment is with very high heat, so directly be passed into that the first water tank 5 is interior will cause the waste of heat, so be provided with a heat exchanger at the first import 1 place, to waste gas, lower the temperature, and the heat of exchange can be used to other place, in waste gas after cooling, some gases directly condense into liquid, reduce the burden of follow-up absorption.
In order well to recycle water resource, exhaust-gas treatment tower bottom is provided with storage tank 14, and the delivery port of storage tank 14 connects filtration system 15, by water pump 16, is connected with the shower 17 in spraying layer 12.
Between dehydration layer 18 and active carbon layer 20, be provided with SCR catalytic unit 19, can further remove oxynitrides in waste gas, guarantee that the gas of discharging meets standard.
It is cylindric that exhaust gas treating tower is, and its air inlet 13 is opened in the tangential direction of exhaust gas treating tower cylinder, can reduce the intake velocity of waste gas, convenient fully processing.
The use procedure of chemical emission treating apparatus is: first, from waste gas, be passed into and in heat exchanger, carry out heat exchange, EGT reduces, and by high boiling gas liquefaction in waste gas, alleviate the burden of subsequent treatment, waste gas is passed in the first water tank 5 by cellular air inlet 3 afterwards, gas is divided into minute bubbles, by narrow meshed dividing plate 2, making gas further divided, can fully contact with water, dust and water-soluble gas are stayed in the first water tank 5, waste gas enters into chemical processing tank 7 afterwards, chemical processing tank 7 packs different treat liquid into according to the different situation of each factory, waste gas also absorbs waste gas and the abundant haptoreaction of chemical liquid by cellular air inlet 3 and narrow meshed dividing plate 2, enter into afterwards in the second water tank 9, in the second water tank 9, again by cellular air inlet 3 and narrow meshed dividing plate 2, be divided into minute bubbles, fully contact with water, waste gas is absorbed from the formed fog of chemical liquid of taking out of in chemical processing tank 7, be passed into afterwards in exhaust gas treating tower exhaust gas velocity is slowed down and again absorbs pernicious gas by spraying layer 12, by dehydration layer 18, waste gas is dry, by SCR catalytic unit 19, process remaining oxynitrides afterwards, afterwards by active carbon layer 20 out after, be discharged in atmospheric environment.
It is emphasized that: be only preferred embodiment of the present invention above, not the present invention is done to any pro forma restriction, any simple modification, equivalent variations and modification that every foundation technical spirit of the present invention is done above embodiment, all still belong in the scope of technical solution of the present invention.
Claims (6)
1. a chemical emission treatment facility, comprise airtight the first water tank (5), the second water tank (9) and chemical processing tank (7), the first outlet (1) of the first water tank (5) is connected with the chemical treatment import (6) of chemical processing tank (7), the chemical treatment outlet (8) of chemical processing tank (7) is connected with second import (10) of the second water tank (9), the second outlet (11) of the second water tank (9) is communicated with the air inlet (13) of exhaust gas treating tower, exhaust gas treating tower inside is provided with spraying layer (12) successively, dehydration layer (18) and active carbon layer (20), first import (1) of described the first water tank (5), chemical treatment import (6) and the second import (10) all extend into below liquid level, it is characterized in that: described the first water tank (5), in the second water tank (9) and chemical processing tank (7), be provided with a dividing plate (2), dividing plate (2) is positioned at below liquid level, described dividing plate (2) is provided with the aperture for bubble is cut apart of array arrangement, described the first import (1), chemical treatment import (6) and the second import (10) are all inserted below dividing plate (2).
2. chemical emission treatment facility according to claim 1, is characterized in that: described the first import (1), chemical treatment import (6) and the second import (10) locate to be provided with cellular gas outlet (3).
3. chemical emission treatment facility according to claim 1, is characterized in that: described the first import (1) locates to be provided with a heat exchanger.
4. chemical emission treatment facility according to claim 1, it is characterized in that: described exhaust-gas treatment tower bottom is provided with storage tank (14), the delivery port of storage tank (14) connects filtration system (15), by water pump (16), is connected with the shower (17) in spraying layer (12).
5. chemical emission treatment facility according to claim 1, is characterized in that: between described dehydration layer (18) and active carbon layer (20), be provided with SCR catalytic unit (19).
6. chemical emission treatment facility according to claim 1, is characterized in that: described exhaust gas treating tower is cylindric, and its air inlet (13) is opened in the tangential direction of exhaust gas treating tower cylinder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310617451.5A CN103599686A (en) | 2013-11-29 | 2013-11-29 | Chemical waste gas treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310617451.5A CN103599686A (en) | 2013-11-29 | 2013-11-29 | Chemical waste gas treatment equipment |
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| CN103599686A true CN103599686A (en) | 2014-02-26 |
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| CN201310617451.5A Pending CN103599686A (en) | 2013-11-29 | 2013-11-29 | Chemical waste gas treatment equipment |
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Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105032097A (en) * | 2015-08-14 | 2015-11-11 | 江苏鼎新印染有限公司 | Air purifying apparatus for textile workshop |
| CN105498403A (en) * | 2016-01-05 | 2016-04-20 | 罗炽良 | Method and system for processing waste gas of internal combustion engine through filtered fluid and purification liquid |
| CN105688624A (en) * | 2016-04-07 | 2016-06-22 | 金柯楠 | Waste gas purifier |
| CN105999964A (en) * | 2016-07-14 | 2016-10-12 | 旌德县龙强净化材料厂 | Waste gas treatment device for preparation of activated carbon from forestry and agricultural waste |
| CN107631318A (en) * | 2017-10-26 | 2018-01-26 | 河南高盛企业管理咨询有限公司 | Removable rubbish emission-control equipment |
| CN107670476A (en) * | 2017-10-26 | 2018-02-09 | 郑州天舜电子技术有限公司 | Novel heating type stench processing system |
| CN108607333A (en) * | 2018-04-26 | 2018-10-02 | 刘兴海 | A kind of waste gas treatment equipment |
| CN109289487A (en) * | 2018-11-02 | 2019-02-01 | 辽宁新瑞碳材料科技有限公司 | A kind of processing method of the high temperature furnace containing chlorine, argon tail gas |
| CN109603385A (en) * | 2018-12-03 | 2019-04-12 | 杭州知桔科技有限公司 | The fume cleaning filter plant of industry environmental protection |
| CN110238153A (en) * | 2019-06-10 | 2019-09-17 | 中国地质大学（武汉） | A kind of volatility organic polluted soil salvage shop exhaust treatment system |
| CN110743335A (en) * | 2018-07-23 | 2020-02-04 | 宁国诚石橡塑制品有限公司 | Rubber and plastic production waste gas treatment equipment |
| CN111111362A (en) * | 2019-12-28 | 2020-05-08 | 江苏新中金环保科技股份有限公司 | Flue gas desulfurization and denitrification complete equipment based on efficient catalysis technology |
| CN114632412A (en) * | 2022-04-25 | 2022-06-17 | 南通久奇环保节能工程有限公司 | Energy-concerving and environment-protective type chemical waste gas sprays equipment |
| CN115253647A (en) * | 2022-09-28 | 2022-11-01 | 江苏大橡木集团有限公司 | Laboratory exhaust treatment device |
| CN114632412B (en) * | 2022-04-25 | 2024-11-15 | 南通久奇环保节能工程有限公司 | Energy-saving and environment-friendly chemical waste gas spraying equipment |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN202715343U (en) * | 2012-08-24 | 2013-02-06 | 东营环安环保科技有限公司 | Spraying absorption tower with a pre-positioned spraying device |
| CN103272465A (en) * | 2013-05-24 | 2013-09-04 | 东华大学 | Portable haze purification device |
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2013
- 2013-11-29 CN CN201310617451.5A patent/CN103599686A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202715343U (en) * | 2012-08-24 | 2013-02-06 | 东营环安环保科技有限公司 | Spraying absorption tower with a pre-positioned spraying device |
| CN103272465A (en) * | 2013-05-24 | 2013-09-04 | 东华大学 | Portable haze purification device |
Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105032097A (en) * | 2015-08-14 | 2015-11-11 | 江苏鼎新印染有限公司 | Air purifying apparatus for textile workshop |
| CN105498403A (en) * | 2016-01-05 | 2016-04-20 | 罗炽良 | Method and system for processing waste gas of internal combustion engine through filtered fluid and purification liquid |
| CN105688624A (en) * | 2016-04-07 | 2016-06-22 | 金柯楠 | Waste gas purifier |
| CN105999964A (en) * | 2016-07-14 | 2016-10-12 | 旌德县龙强净化材料厂 | Waste gas treatment device for preparation of activated carbon from forestry and agricultural waste |
| CN107631318A (en) * | 2017-10-26 | 2018-01-26 | 河南高盛企业管理咨询有限公司 | Removable rubbish emission-control equipment |
| CN107670476A (en) * | 2017-10-26 | 2018-02-09 | 郑州天舜电子技术有限公司 | Novel heating type stench processing system |
| CN107631318B (en) * | 2017-10-26 | 2019-08-06 | 上海启菲特环保生物技术有限公司 | Removable rubbish emission-control equipment |
| CN108607333A (en) * | 2018-04-26 | 2018-10-02 | 刘兴海 | A kind of waste gas treatment equipment |
| CN110743335A (en) * | 2018-07-23 | 2020-02-04 | 宁国诚石橡塑制品有限公司 | Rubber and plastic production waste gas treatment equipment |
| CN109289487A (en) * | 2018-11-02 | 2019-02-01 | 辽宁新瑞碳材料科技有限公司 | A kind of processing method of the high temperature furnace containing chlorine, argon tail gas |
| CN109289487B (en) * | 2018-11-02 | 2021-06-29 | 辽宁新瑞碳材料科技有限公司 | Method for treating chlorine and argon-containing tail gas of high-temperature furnace |
| CN109603385A (en) * | 2018-12-03 | 2019-04-12 | 杭州知桔科技有限公司 | The fume cleaning filter plant of industry environmental protection |
| CN110238153A (en) * | 2019-06-10 | 2019-09-17 | 中国地质大学（武汉） | A kind of volatility organic polluted soil salvage shop exhaust treatment system |
| CN111111362A (en) * | 2019-12-28 | 2020-05-08 | 江苏新中金环保科技股份有限公司 | Flue gas desulfurization and denitrification complete equipment based on efficient catalysis technology |
| CN111111362B (en) * | 2019-12-28 | 2021-05-25 | 江苏新中金环保科技股份有限公司 | Flue gas desulfurization and denitrification complete equipment based on efficient catalysis technology |
| CN114632412A (en) * | 2022-04-25 | 2022-06-17 | 南通久奇环保节能工程有限公司 | Energy-concerving and environment-protective type chemical waste gas sprays equipment |
| CN114632412B (en) * | 2022-04-25 | 2024-11-15 | 南通久奇环保节能工程有限公司 | Energy-saving and environment-friendly chemical waste gas spraying equipment |
| CN115253647A (en) * | 2022-09-28 | 2022-11-01 | 江苏大橡木集团有限公司 | Laboratory exhaust treatment device |
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Application publication date: 20140226 |