CN1242257A - Active carbon fiber for removing foul smell gas, and method for preparing same - Google Patents
Active carbon fiber for removing foul smell gas, and method for preparing same Download PDFInfo
- Publication number
- CN1242257A CN1242257A CN 99101504 CN99101504A CN1242257A CN 1242257 A CN1242257 A CN 1242257A CN 99101504 CN99101504 CN 99101504 CN 99101504 A CN99101504 A CN 99101504A CN 1242257 A CN1242257 A CN 1242257A
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- nacf
- carbon fiber
- active carbon
- foul gas
- copper
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Abstract
Said method for prepn. of active carbon cellulose is to dry active carbon cellulose under 100-150 deg.C, then impregnate in 0.5-10% copper salt solution for 0.5-24 hr. then treat in air or inert gas atmosphere at 100-450 deg.C for 2-10 hr. to obtain the deodirizing material. The advantages include in pollution, low cost, good deodorization effect, etc.
Description
The invention belongs to a kind of material that removes foul gas, relate in particular to a kind of NACF that removes foul gas and preparation method thereof.
In recent years, an importance as environmental pollution improvement, the improvement of the odor pollution of commercial production and living facilities also has been subjected to unprecedented attention, processing material at odor pollution constantly is developed, people have at first developed the sensation deodorizing method, promptly shelter foul smell with discharging the aromatic series material, this method is simple and convenient, but is not that the basic method foul smell that effects a radical cure also exists in air, and scientific and technical personnel develop chemical deodorizing method again, promptly be to pass through oxidizing process, firing method, chemical reactions such as chemical reagent absorption process are handled foul smell, and this method has high selectivity, but there is secondary pollution, the shortcoming that service life is short.
In order to overcome above-mentioned shortcoming, people develop microbial decomposition foul gas molecule and catalyzed conversion foul smell molecule process again, but there is the higher shortcoming of cost, so scientific and technical personnel develop the absorbing and deodorizing method, promptly utilize active carbon or silica gel that the foul gas molecule is carried out physics or chemisorbed, but exist dynamic adsorption capacity relatively poor, the shortcoming that adsorption capacity is less.
Goal of the invention of the present invention provides a kind of pollution-free; Cost is low, and absorbability is big removes NACF of foul gas and preparation method thereof.
The object of the present invention is achieved like this, handle NACF with certain density copper salt solution, Low Temperature Heat Treatment certain hour under certain atmosphere then, make the deodorize material, because the activated carbon fiber-loaded active ingredient copper that goes up, make it that deodorizing performance is big have been improved, so just improved the ratio of performance to price, be applicable to suitability for industrialized production.
Composition of the present invention is (percentage by weight)
NACF 92-98% Cu 2-8%
Its physical property is specific surface area (m
2/ g) 200-1000
Pore volume (cc/g) 0.1-0.4
The physical property of aforesaid NACF is:
Specific surface area (m
2/ g) 500-1200
Pore volume (cc/g) 0.2-0.6
Aforesaid NACF is a polyacrylonitrile radical active carbon fiber, viscose glue base activated fibre, asphalt based active carbon fiber, phenolic resin based activated carbon fiber.
Aforesaid Cu is the simple substance of copper, Cu oxide, copper sulfide.
Preparation method of the present invention be with NACF the 100-150 ℃ of down dry back working concentration mantoquita impregnation process that is 0.5-10% 0.5-24 hour, then in air or inert atmosphere, handle the deodorize material that made in 2-10 hour under 100-450 ℃ of temperature.
The deoxidation material that the present invention makes is applicable to the processing of sulfur series foul smell gas by using gas.
The present invention compared with prior art has following advantage:
(1) pollution-free.
(2) cost is low.
(3) deodorising effect is good.
(4) under situation about suitably raising the cost, improved the ratio of performance to price greatly.
Embodiment 1
With specific surface area is 800m
2/ g, pore volume is that the polyacrylonitrile radical active carbon fiber of 0.4cc/g is dry down at 120 ℃, be to flood 10 hours in the 1% Schweinfurt green solution then in concentration, taking-up is extracted, 150 ℃ of following Low Temperature Heat Treatment make the deodorize material in air atmosphere, and it consists of: NACF 96%, copper 4%, physical property: specific surface area is 850m
2/ g; Pore volume is 0.45cc/g.Performance test: use this material of 1.5g in room temperature, anaerobic, dynamic adsorption is handled the odor pollution dusty gas under the exsiccant condition, the hydrogen sulfide entrance concentration is 500ppm, the methanthiol entrance concentration is the contamination gas (nitrogen+hydrogen sulfide+methanthiol) (flow is 350ml/min) of 500ppm, time of break-through (exit concentration is that the adsorption time of entrance concentration 5% is a time of break-through) is respectively: hydrogen sulfide 60 hours, mercaptan 70 hours, and the time of break-through of the not modified polyacrylonitrile NACF under the same terms has only 8 hours (to hydrogen sulfide), 6 hours (to mercaptan).
Embodiment 2
With specific surface area is 700m
2/ g, pore volume is that the polyacrylonitrile radical active carbon fiber of 0.3cc/g is dry down at 120 ℃, be to flood 10 hours in the 1% Schweinfurt green solution then in concentration, taking-up is extracted, 150 ℃ of following Low Temperature Heat Treatment make the deodorize material in air atmosphere, and it consists of: NACF 98%, copper 2%, physical property: specific surface area is 800m
2/ g, pore volume are 0.35cc/g.Performance test: use this material of 1.5g in room temperature, anaerobic, adsorption treatment odor pollution gas under the condition of low humidity (5%), the hydrogen sulfide entrance concentration is 500ppm, the methanthiol entrance concentration is the contamination gas (nitrogen+hydrogen sulfide+methanthiol) (flow is 350ml/min) of 500ppm, time of break-through (exit concentration be 5% o'clock be time of break-through) is respectively: hydrogen sulfide 52 hours, mercaptan 78 hours, the time of break-through of viscose-based active carbon fiber only is hydrogen sulfide 1.5 hours respectively under the same conditions, mercaptan 1.8 hours.
Claims (5)
1. a NACF that is used to remove foul gas is characterized in that composition is (percentage by weight)
NACF 92-98% Cu 2-8%
Its physical property is specific surface area (m
2/ g) 200-1000
Pore volume (cc/g) 0.1-0.4
2. a kind of NACF that is used to remove foul gas according to claim 1 is characterized in that the physical property of the NACF that connected is:
Specific surface area (m
2/ g) 500-1200
Pore volume (cc/g) 0.2-0.6
3. a kind of NACF that is used to remove foul gas according to claim 1 and 2 is characterized in that described NACF is a polyacrylonitrile radical active carbon fiber, viscose glue base activated fibre, asphalt based active carbon fiber, phenolic resin based activated carbon fiber.
4. a kind of NACF that is used to remove foul gas according to claim 1 is characterized in that described Cu is the simple substance of copper, the oxide of copper, the sulfide of copper.
5. preparation method that is used to remove the NACF of foul gas, it is characterized in that NACF the 100-150 ℃ of down dry back working concentration mantoquita impregnation process that is 0.5-10% 0.5-24 hour, then in air or inertia, handled 2-10 hour the deodorize material that makes under the 100-450 ℃ of temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99101504A CN1108861C (en) | 1999-01-01 | 1999-01-01 | Active carbon fiber for removing foul smell gas, and method for preparing same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99101504A CN1108861C (en) | 1999-01-01 | 1999-01-01 | Active carbon fiber for removing foul smell gas, and method for preparing same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1242257A true CN1242257A (en) | 2000-01-26 |
| CN1108861C CN1108861C (en) | 2003-05-21 |
Family
ID=5270485
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN99101504A Expired - Fee Related CN1108861C (en) | 1999-01-01 | 1999-01-01 | Active carbon fiber for removing foul smell gas, and method for preparing same |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1108861C (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100417438C (en) * | 2005-12-09 | 2008-09-10 | 侯立安 | CS2 adsorbing material and its prepn method and application |
| CN101496993B (en) * | 2009-01-07 | 2011-06-22 | 上海水天环保科技有限公司 | Method and device for processing malodorous gas by active bamboo charcoal-H2O2 complex phase catalytic oxidation |
| CN102059048B (en) * | 2009-01-07 | 2013-03-20 | 上海水天环保科技有限公司 | Method for treating obnoxious gas by active bamboo charcoal-H2O2 composite catalytic oxidation |
| CN110860179A (en) * | 2019-12-04 | 2020-03-06 | 燕山大学 | Formaldehyde scavenging agent and preparation method thereof |
| CN115400730A (en) * | 2022-10-17 | 2022-11-29 | 中国兵器装备集团西南技术工程研究所 | Corrosive atmosphere absorbing material, preparation method and application thereof |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5777019A (en) * | 1980-10-30 | 1982-05-14 | Toho Rayon Co Ltd | Fibrous activated carbon and its manufacture |
| US5102855A (en) * | 1990-07-20 | 1992-04-07 | Ucar Carbon Technology Corporation | Process for producing high surface area activated carbon |
-
1999
- 1999-01-01 CN CN99101504A patent/CN1108861C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100417438C (en) * | 2005-12-09 | 2008-09-10 | 侯立安 | CS2 adsorbing material and its prepn method and application |
| CN101496993B (en) * | 2009-01-07 | 2011-06-22 | 上海水天环保科技有限公司 | Method and device for processing malodorous gas by active bamboo charcoal-H2O2 complex phase catalytic oxidation |
| CN102059048B (en) * | 2009-01-07 | 2013-03-20 | 上海水天环保科技有限公司 | Method for treating obnoxious gas by active bamboo charcoal-H2O2 composite catalytic oxidation |
| CN110860179A (en) * | 2019-12-04 | 2020-03-06 | 燕山大学 | Formaldehyde scavenging agent and preparation method thereof |
| CN110860179B (en) * | 2019-12-04 | 2021-10-26 | 燕山大学 | Formaldehyde scavenging agent and preparation method thereof |
| CN115400730A (en) * | 2022-10-17 | 2022-11-29 | 中国兵器装备集团西南技术工程研究所 | Corrosive atmosphere absorbing material, preparation method and application thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1108861C (en) | 2003-05-21 |
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