CN1792438A - Catalyst for treating benzene series organic waste-gas or waste-water by using low temp. and dry method, prepn. method and application thereof - Google Patents
Catalyst for treating benzene series organic waste-gas or waste-water by using low temp. and dry method, prepn. method and application thereof Download PDFInfo
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- CN1792438A CN1792438A CN 200510048220 CN200510048220A CN1792438A CN 1792438 A CN1792438 A CN 1792438A CN 200510048220 CN200510048220 CN 200510048220 CN 200510048220 A CN200510048220 A CN 200510048220A CN 1792438 A CN1792438 A CN 1792438A
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- active carbon
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Abstract
A catalyst for treating the benzene contained organic waste gas and the benzene and benzoate contained sewage by low-temp dry method contains metal (1-10 Wt%) chosen from Cu, Fe, V and Co, and activated carbon (90-99 Wt%) as carrier. Its application includes such steps as passing said waste gas or sewage through said catalyst while adsorbing, drying, filling oxidizing gas and reaction.
Description
Technical field
The invention belongs to a kind of absorption-catalyst and application process thereof, relating in particular to a kind of is absorption-catalyst and the preparation method and the using method of active component with the transition metal.
Background technology:
Oil, chemical industry and coking give off the industrial wastewater that contains toluene, dimethylbenzene, ethylbenzene and benzoate in a large number in producing.U.S. environment administration classifies toluene, ethylbenzene and dimethylbenzene (BTEX) as priority pollutant, and they have toxicity to various life forms.These pollutants can be found in contaminated underground water.Toluene, dimethylbenzene and ethylbenzene belong to volatile organic contaminant (VOCs) simultaneously, and biology is had very strong toxic action, thus these waste gas and waste water necessary processing the before discharging, to reduce pollution to environment.And toluene, dimethylbenzene, ethylbenzene and benzoate belong to the pollutant of difficult for biological degradation, and general water technology is difficult to handle this type of waste water.At present, the adsorption technology based on the good absorption property of active carbon has a wide range of applications at organic wastewater and exhaust-gas treatment field.(89:20), visible active carbon has the good adsorption performance to this type organic for Environ.Sci.Technol.1994,28:1403 and Chem.Eng.Progr.1993 can effectively to handle VOCs in the waste gas with active carbon as adsorbent.But after in a single day the adsorption capacity of active carbon reaches capacity, just need handle so that utilize again it.Regeneration techniques commonly used is heat regeneration in the industry at present.In the hot regenerative process, the active carbon that adsorbs after saturated will be handled under the high temperature of 800-850oC, and energy consumption is big; Simultaneously, high-temperature operation makes that the adsorption capacity loss late of active carbon is big, a charcoal absorption capacitance loss of every regeneration 5-15%; In addition, high-temperature operation also makes active carbon can not carry out in-situ regeneration, needs specific regenerating unit, thereby increases disposal cost and cause a certain amount of active carbon loss in transportation; At last, the pollutant of desorption also needs post processing, complex process in the heating process.
Summary of the invention
The object of the present invention is to provide a kind of active high, technology simply be suitable for handling the benzene series organic exhaust gas or contain the benzene series organic matter and benzoate waste water be absorption-catalyst and preparation method's and methods for using them of carrier with the active carbon.
On active carbon, support a certain amount of metal oxide and make metal/charcoal (AC) absorption-catalyst, utilize the good absorption property of active carbon to purify liquid waste, pollutant is concentrated, be blown into hot-air after the draining, utilize the catalytic activity and the selectivity of catalyst, under temperate condition,, be a kind of feasible and cost-effective method of wastewater treatment thereby make the low temperature dry method catalytic oxidation of active carbon regeneration with adsorbed contaminants oxidative degradation.
Absorption-catalyst provided by the invention contains a kind of among transition metal Cu, Fe, V, the Co, and it is to be carrier with the active carbon, and the percentage by weight of its component is: metal 1%-10%, active carbon are 90-99%, and the surface area of active carbon is 500-1500m
2/ g.
Absorption-method for preparing catalyst provided by the invention is an equi-volume impregnating, with a kind of nitrate solution incipient impregnation absorbent charcoal carrier among transition metal Cu, Fe, V or the Co, place 4-6h in room temperature, then at 50-100 ℃ of dry 6-24 hour, calcined 6-24 hour under 200-500 ℃ of inert atmosphere at last, obtaining with the active carbon is the absorption-catalyst of carrier.
Absorption provided by the invention-Application of Catalyst method for the organic wastewater that will contain the benzene series organic exhaust gas or contain benzene series organic matter and benzoate by being the absorption-catalyst of carrier with the active carbon, after absorption finishes, dry at normal temperatures, feed oxidizing gas, air speed is 500-2000h
-1, be 200-350 ℃ in reaction temperature, reaction 1-3h, cycle applications afterwards.
The indegradable industrial effluent that this absorption-catalyst is specially adapted to handle the benzene series organic exhaust gas or contains benzene series organic matter and benzoate.Technology of the present invention also be fit to handle similarly other organic exhaust gas or the industrial wastewater of difficult degradation.
The present invention has compared following advantage with prior art:
1. absorption-catalyst has the good adsorption performance.Can adsorb in waste gas and the waste water various benzene series organic matters and or pollutant such as Sodium Benzoate efficiently.
2. the catalytic oxidation mild condition is carried out under the low-temperature atmosphere-pressure, need not a large amount of water body heating pressurizations, energy consumption is low, and occupation area of equipment is little, and process is simple, simple to operate, but in-situ catalytic oxidation does not produce secondary pollution, and it is not high to be particularly suitable for concentration of treatment, but toxicity is big, be unsuitable for the waste water of biochemical treatment, and the waste water of handling can reuse, has saved a large amount of water for industrial uses.
3. absorbent charcoal based absorption-catalyst of supporting of transition metal can use behind the catalytic oxidation continuously, easily generates in batch on a large scale and uses, and cost is low.
The specific embodiment
Embodiment 1.
Cu5/AC. Preparation of catalysts:
Getting the copper nitrate solution 100ml of 0.78mol/l, is 800m with 100 gram 40-60 order specific areas
2The activated carbon granule of/g is poured in the maceration extract and is stirred; room temperature was placed 4 hours; dried 6 hours down in 110 ℃; calcined 12 hours down in 250 ℃ of argon shields again; naturally cool to room temperature and make catalyst A; the weight of metal component is in the catalyst A: Cu 5%, and active carbon is 95%, is labeled as Cu5/AC.
The use of Cu5/AC absorption-catalyst:
The organic wastewater 50ml that will contain 100ppm ethylbenzene and 100ppm Sodium Benzoate is by being equipped with the adsorption column of 0.5gCu5/AC absorption-catalyst, absorption finishes the waste water that the back discharging is cleaned, the Cu5/AC absorption-catalyst of dry at normal temperatures absorption ethylbenzene and Sodium Benzoate; Give in the dried Cu5/AC absorption-catalyst and feed oxidizing gas (5% oxygen), air speed is 1000h
-1, and temperature risen to 280 ℃; 280 ℃ of following constant temperature catalytic oxidations 1.5 hours.Catalytic oxidation reduces the temperature to room temperature after finishing in oxidizing atmosphere.
Experimental result: ethylbenzene in the waste water and Sodium Benzoate can get 100% removal, Cu5/AC absorption-catalyst after the regeneration can adsorb in the organic wastewater that 50ml contains 100ppm ethylbenzene and 100ppm Sodium Benzoate 100% ethylbenzene and Sodium Benzoate once more, online Mass Spectrometer Method repeatedly in the cyclic process pollutant catalyzing oxidizing degrading product be CO
2And H
2O.
Embodiment 2
The Fe5/AC Preparation of catalysts:
Getting the iron nitrate solution 100ml of 0.89mol/l, is 1200m with 100 gram 40-60 order specific areas
2The activated carbon granule of/g is poured in the maceration extract and is stirred; room temperature was placed 6 hours; dried 12 hours down in 110 ℃; calcined 24 hours down in 300 ℃ of argon shields again; naturally cool to room temperature and make catalyst B; the weight of metal component is in the catalyst B: Fe 5%, and active carbon is 95%, is labeled as Fe5/AC.
The use of Fe5/AC absorption-catalyst:
The organic wastewater 100ml that will contain 100ppm ethylbenzene and 100ppm Sodium Benzoate is by being equipped with the adsorption column of 0.5gFe5/AC absorption-catalyst, absorption finishes the waste water that the back discharging is cleaned, the Fe5/AC absorption-catalyst of dry at normal temperatures absorption toluene and Sodium Benzoate; Give in the dried Fe5/AC absorption-catalyst and feed oxidizing gas (5% oxygen), air speed is 500h
-1, and temperature risen to 300 ℃; 300 ℃ of following constant temperature catalytic oxidations 2 hours, the constant temperature catalytic oxidation reduced the temperature to room temperature after finishing in oxidizing atmosphere.
Experimental result: toluene in the waste water and Sodium Benzoate can be near 100% removals, Fe5/AC absorption-catalyst after the regeneration can adsorb in the organic wastewater that 100ml contains 100ppm ethylbenzene and 100ppm Sodium Benzoate 100% ethylbenzene and Sodium Benzoate once more, online Mass Spectrometer Method repeatedly in the cyclic process pollutant catalyzing oxidizing degrading product be CO
2And H
2O.
Embodiment 3
The V5/AC Preparation of catalysts:
With 40-60 order specific area is 500m
2The activated carbon granule dipping ammonium metavanadate of/g and the mixed solution (wherein the concentration of ammonium metavanadate is 0.043g/ml) of oxalic acid, room temperature was placed 6 hours, dried 24 hours down in 110 ℃, oxidation in calcining and the air in inert atmosphere successively then, naturally cool to room temperature and make catalyst C, the weight of metal component is among the catalyst C: V 5%, and active carbon is 95%, is labeled as V5/AC.
The use of V5/AC absorption-catalyst:
The 10L organic exhaust gas room temperature that will contain 5ppm toluene, 5ppm ethylbenzene and 5ppm dimethylbenzene is by being equipped with the bed of 0.5gV5/AC absorption-catalyst, the absorption of V5/AC absorption-catalyst toluene, ethylbenzene and dimethylbenzene; To feeding oxidizing gas (5% oxygen) in the V5/AC absorption-catalyst, air speed is 1000h
-1, and temperature risen to 200 ℃; 200 ℃ of following constant temperature catalytic oxidations 1 hour, the constant temperature catalytic oxidation reduced the temperature to room temperature after finishing in oxidizing atmosphere.
Experimental result: the toluene in the waste gas, ethylbenzene and dimethylbenzene can get 100% removal, Fe5/AC absorption-catalyst after the regeneration can adsorb in the organic exhaust gas that 10L contains 5ppm toluene, 5ppm ethylbenzene and 5ppm dimethylbenzene 100% toluene, ethylbenzene and dimethylbenzene once more, online Mass Spectrometer Method repeatedly in the cyclic process pollutant catalyzing oxidizing degrading product be CO
2And H
2O.
Embodiment 4.
V2/AC absorption-Preparation of catalysts:
Concrete preparation method is identical with embodiment 3, is prepared into the catalyst D that contains V2%, and wherein the weight of metal component is: V is 2%, and active carbon is 98%, is labeled as V2/AC.
The use of V2/AC absorption-catalyst:
The 10L organic exhaust gas room temperature that will contain 5ppm toluene, 5ppm ethylbenzene and 5ppm dimethylbenzene is by being equipped with 0.5gV2/AC absorption-beds, the absorption of V2/AC absorption-catalyst toluene, ethylbenzene and dimethylbenzene; To feeding oxidizing gas (5% oxygen) in the V2/AC absorption-catalyst, air speed is 2000h
-1, and temperature risen to 250 ℃; 250 ℃ of following constant temperature catalytic oxidations 1.5 hours, the constant temperature catalytic oxidation reduced the temperature to room temperature after finishing in oxidizing atmosphere.
Experimental result: the toluene in the waste gas, ethylbenzene and dimethylbenzene can get 100% removal, V2/AC absorption-catalyst after the regeneration can adsorb 100% toluene, ethylbenzene and the dimethylbenzene in the organic exhaust gas that 10L contains 5ppm toluene, 5ppm ethylbenzene and 5ppm dimethylbenzene once more, online Mass Spectrometer Method repeatedly in the cyclic process pollutant catalyzing oxidizing degrading product be CO
2And H
2O.
Embodiment 5
The Co8/AC Preparation of catalysts:
Getting the cobalt nitrate solution 100ml of 1.36mol/l, is 1000m with 100 gram 40-60 order specific areas
2The activated carbon granule of/g is poured in the maceration extract and is stirred, and room temperature was placed 4 hours, dries 6 hours down in 110 ℃; calcined 12 hours down in argon shield, naturally cool to room temperature and make catalyst E, the weight of metal component is among the catalyst E: Co 8%; active carbon is 92%, is labeled as Co8/AC.
The use of Co8/AC absorption-catalyst:
The organic wastewater 50ml that contains 100ppm ethylbenzene and 100ppm Sodium Benzoate is by being equipped with the adsorption column of 0.5gCo8/AC absorption-catalyst, absorption finishes the waste water that the back discharging is cleaned, the Co8/AC absorption-catalyst of dry at normal temperatures absorption ethylbenzene and Sodium Benzoate; Give in the dried Co8/AC absorption-catalyst and feed oxidizing gas (5% oxygen), air speed is 1500h
-1, and temperature risen to 250 ℃; 250 ℃ of following constant temperature catalytic oxidations 2 hours.Catalytic oxidation reduces the temperature to room temperature after finishing in oxidizing atmosphere.
Experimental result: ethylbenzene in the waste water and Sodium Benzoate can get 100% removal, Co8/AC absorption-catalyst after the regeneration can adsorb in the organic wastewater that 50ml contains 100ppm ethylbenzene and 100ppm Sodium Benzoate 100% ethylbenzene and Sodium Benzoate once more, online Mass Spectrometer Method repeatedly in the cyclic process pollutant catalyzing oxidizing degrading product be CO
2And H
2O.
Embodiment 6
The Co1/AC Preparation of catalysts:
Getting the cobalt nitrate solution 100ml of 0.17mol/l, is 1000m with 100 gram 40-60 order specific areas
2The activated carbon granule of/g is poured in the maceration extract and is stirred; room temperature was placed 4 hours; dried 6 hours down in 110 ℃; calcined 12 hours down in 300 ℃ of argon shields again; naturally cool to room temperature and make catalyst F; the weight of metal component is among the catalyst F: Co1%, active carbon is 99%, is labeled as Co1/AC.
The use of Co1/AC absorption-catalyst:
The organic wastewater 100ml that will contain 100ppm ethylbenzene and 100ppm Sodium Benzoate is by being equipped with the adsorption column of 0.5g Co1/AC absorption-catalyst, absorption finishes the waste water that the back discharging is cleaned, the Co1/AC absorption-catalyst of dry at normal temperatures absorption toluene and Sodium Benzoate; Give in the dried Co1/AC absorption-catalyst and feed oxidizing gas (5% oxygen), air speed is 1500h
-1, and temperature risen to 250 ℃; 250 ℃ of following constant temperature catalytic oxidations 2 hours, the constant temperature catalytic oxidation reduced the temperature to room temperature after finishing in oxidizing atmosphere.
Experimental result: toluene in the waste water and Sodium Benzoate can be near 100% removals, Co1/AC absorption-catalyst after the regeneration can adsorb in the organic wastewater that 100ml contains 100ppm ethylbenzene and 100ppm Sodium Benzoate 100% ethylbenzene and Sodium Benzoate once more, online Mass Spectrometer Method repeatedly in the cyclic process pollutant catalyzing oxidizing degrading product be mainly CO
2And H
2O has the effusion of micro-benzene.
Claims (3)
1, the catalyst of a kind of low temperature dry process benzene series organic exhaust gas or waste water, the percentage by weight that it is characterized in that catalyst consists of: metal 1%-10%, active carbon is 90-99%, and wherein metal is Cu, Fe, V or Co, and the surface area of active carbon is 500-1500m
2/ g.
2, the Preparation of catalysts method of a kind of according to claim 1 low temperature dry process benzene series organic exhaust gas or waste water, it is characterized in that transition metal Cu, Fe, V or Co nitrate solution incipient impregnation absorbent charcoal carrier, place 4-6h in room temperature, then at 50-100 ℃ of dry 6-24 hour, calcined 6-24 hour under 200-500 ℃ of inert atmosphere at last, obtaining with the active carbon is the absorption-catalyst of carrier.
3, the Application of Catalyst method of a kind of according to claim 1 low temperature dry process benzene series organic exhaust gas or waste water, it is characterized in that the organic wastewater that will contain the benzene series organic exhaust gas or contain benzene series organic matter and benzoate is by being the absorption-catalyst of carrier with the active carbon, after absorption finishes, dry at normal temperatures, feed oxidizing gas, air speed is 500-2000h
-1, be 200-350 ℃ in reaction temperature, reaction 1-3h, cycle applications afterwards.
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|---|---|---|---|
| CNB2005100482202A CN100354041C (en) | 2005-12-21 | 2005-12-21 | Catalyst for treating benzene series organic waste-gas or waste-water by using low temp. and dry method, prepn. method and application thereof |
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|---|---|---|---|
| CNB2005100482202A CN100354041C (en) | 2005-12-21 | 2005-12-21 | Catalyst for treating benzene series organic waste-gas or waste-water by using low temp. and dry method, prepn. method and application thereof |
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| CN101406838B (en) * | 2008-11-20 | 2011-06-08 | 武汉大学 | Method for preparing active carbon supported ferriferous oxide catalyst and wastewater treatment system thereof |
| CN102500391A (en) * | 2011-12-19 | 2012-06-20 | 浙江省环境保护科学设计研究院 | Catalyst for non-biodegradable wastewater treatment and preparation method thereof |
| CN103191743A (en) * | 2013-04-19 | 2013-07-10 | 重庆工商大学 | Co-based supported catalyst for catalytic removal of benzene-series compounds in air and preparation method thereof |
| CN104801272A (en) * | 2015-04-15 | 2015-07-29 | 南通职业大学 | Preparation method of cobalt-supported activated carbon as well as condition and device for adsorbing methylbenzene with cobalt-supported activated carbon |
| CN105642325A (en) * | 2016-01-12 | 2016-06-08 | 陕西科技大学 | Supported vanadium-based catalyst and preparation method thereof |
| CN106315818A (en) * | 2016-09-23 | 2017-01-11 | 郑州航空工业管理学院 | Application of V2O5/CeO2 composite nano-material in degradation of cefalexin-containing wastewater |
| CN108187613A (en) * | 2017-12-20 | 2018-06-22 | 北京汇能兴业科技有限公司 | One kind is suitable for the regenerated Adsorption of Organic agent of high-temperature S removal |
| CN117019118A (en) * | 2023-10-08 | 2023-11-10 | 西安金沃泰环保科技有限公司 | Filtering material for benzene series waste gas and preparation method thereof |
Family Cites Families (3)
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| US5510524A (en) * | 1995-02-21 | 1996-04-23 | Bp Chemicals Limited | Process for the production of a carboxylic acid |
| CN1089034C (en) * | 1999-04-30 | 2002-08-14 | 中国科学院山西煤炭化学研究所 | Desulfurization catalyst of flue gas and its application method |
| CN1102435C (en) * | 1999-04-30 | 2003-03-05 | 中国科学院山西煤炭化学研究所 | Catalyst for removing nitrogen oxide from flue gas, its preparation and application |
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2005
- 2005-12-21 CN CNB2005100482202A patent/CN100354041C/en not_active Expired - Fee Related
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| CN101406838B (en) * | 2008-11-20 | 2011-06-08 | 武汉大学 | Method for preparing active carbon supported ferriferous oxide catalyst and wastewater treatment system thereof |
| CN102500391A (en) * | 2011-12-19 | 2012-06-20 | 浙江省环境保护科学设计研究院 | Catalyst for non-biodegradable wastewater treatment and preparation method thereof |
| CN103191743A (en) * | 2013-04-19 | 2013-07-10 | 重庆工商大学 | Co-based supported catalyst for catalytic removal of benzene-series compounds in air and preparation method thereof |
| CN103191743B (en) * | 2013-04-19 | 2015-06-03 | 重庆工商大学 | Co-based supported catalyst for catalytic removal of benzene-series compounds in air and preparation method thereof |
| CN104801272A (en) * | 2015-04-15 | 2015-07-29 | 南通职业大学 | Preparation method of cobalt-supported activated carbon as well as condition and device for adsorbing methylbenzene with cobalt-supported activated carbon |
| CN105642325A (en) * | 2016-01-12 | 2016-06-08 | 陕西科技大学 | Supported vanadium-based catalyst and preparation method thereof |
| CN106315818A (en) * | 2016-09-23 | 2017-01-11 | 郑州航空工业管理学院 | Application of V2O5/CeO2 composite nano-material in degradation of cefalexin-containing wastewater |
| CN108187613A (en) * | 2017-12-20 | 2018-06-22 | 北京汇能兴业科技有限公司 | One kind is suitable for the regenerated Adsorption of Organic agent of high-temperature S removal |
| CN117019118A (en) * | 2023-10-08 | 2023-11-10 | 西安金沃泰环保科技有限公司 | Filtering material for benzene series waste gas and preparation method thereof |
| CN117019118B (en) * | 2023-10-08 | 2024-01-05 | 西安金沃泰环保科技有限公司 | Filtering material for benzene series waste gas and preparation method thereof |
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