KR890008020A - 활성탄의 제조방법 - Google Patents
활성탄의 제조방법 Download PDFInfo
- Publication number
- KR890008020A KR890008020A KR1019880014771A KR880014771A KR890008020A KR 890008020 A KR890008020 A KR 890008020A KR 1019880014771 A KR1019880014771 A KR 1019880014771A KR 880014771 A KR880014771 A KR 880014771A KR 890008020 A KR890008020 A KR 890008020A
- Authority
- KR
- South Korea
- Prior art keywords
- granules
- activated carbon
- producing activated
- carbonized
- particles
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B32/00—Carbon; Compounds thereof
- C01B32/30—Active carbon
- C01B32/354—After-treatment
- C01B32/384—Granulation
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
내용 없음
Description
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제 1 도는 출발물질인 석탄의 분쇄입자를 평균 입자 크기와 수득된 활성탄의 경도의 관계를 나타내는 그래프이다.
제 2 도는 얄루른 탄(Yallourn coal) 및 세레존 탄(Cerrejon coal)의 분량과 수득된 활성탄의 경도 및 흡착된 요오드의 양 각각의 상호관계를 타나내는 그래프이다.
Claims (10)
- (a) 지점결탄을 10㎛ 이하의 평균 입자 크기를 갖는 분쇄입자로 분쇄하는 분쇄단계 ; (b) 수득된 분쇄 입자를 과립으로 과립화하는 과립화단계 ; (c) 수득된 과립을 탄화하는 탄화단계 ; (d) 수득된 탄화과립을 활성화하는 단계로 구성됨을 특징으로 하는 활성탄의 제조방법.
- 제 1 항에 있어서, 과립화 단계에서 물 및 점도가 낮고 가열 후에 탄소 잔류물 함량이 낮은 탄화수소 오일로 이루어지는 군에서 선택된 결합제를 사용한 활성탄의 제조방법.
- 제 1 항에 있어서, 과립화 단계에서 분쇄 입자를 0.5㎜ 이상의 입자 크기 및 높은 구형도를 갖는 구형 과립으로 과립화하는 활성탄의 제조방법.
- 제 1 항에 있어서, 탄화 단계에서, 과립을 비활성 기체압하에 500∼1000℃의 온도에서 가열함으로써 탄화를 수행하는 활성탄의 제조방법.
- 제 1 항에 있어서, 활성탄 단계에서 탄화된 과립의 활성화가 온도 800∼1000℃, 활성제의 양 : 탄화된 과립 1㎏당 1∼10㎏의 수증기, 및 활성화 시간 : 1∼10시간인 조건하에 수행되는 활성탄의 제조방법.
- (a) 비점결탄, 및 석탄 조성물중의 함량이 40% 이하인 점결탄으로 이루어지는 석탄 조성물을 10㎛ 이하의 평균입자 크기를 갖는 분쇄 입자로 분쇄하는 분쇄단계 ; (b) 수득된 분쇄입자를 과립으로 과립화하는 과립화단계 ; (c) 수득된 과립을 탄화하는 탄화 단계 ; 및 (d) 수득된 탄화 과립을 활성화하는 활성화단계로 구성됨을 특징으로 하는 활성탄의 제조방법.
- 제 6 항에 있어서, 과립화 단계에서 물 및 점도가 낮고 가열후에 탄소 잔류물 함량이 낮은 탄화수소오일로 이루어지는 군에서 선택된 결합제를 사용하는 활성탄의 제조방법.
- 제 6 항에 있어서, 과립화 단계에서 분쇄입자를 0.5㎜ 이사의 입자 크기 및 높은 구형도를 갖는 구형 과립으로 과립화하는 활성탄의 제조방법.
- 제 6 항에 있어서, 탄화 단계에서, 과립을 비활성 기체압하에 500∼1000℃의 온도에서 가열함으로써 탄화를 수행하는 활성탄의 제조방법.
- 제 6 항에 있어서, 활성탄 단계에서 탄화된 과립의 활성화가 온도 800∼1000℃, 활성제의 양 : 탄화된 과립 1㎏당 1∼10㎏의 수증기, 및 활성화 시간 : 1∼10시간인 조건하에 수행되는 활성탄의 제조방법.※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62282152A JPH01126214A (ja) | 1987-11-10 | 1987-11-10 | 球状活性炭の製造方法 |
JP62-282152 | 1987-11-10 | ||
JP62-282,152 | 1987-11-10 |
Publications (2)
Publication Number | Publication Date |
---|---|
KR890008020A true KR890008020A (ko) | 1989-07-08 |
KR910003342B1 KR910003342B1 (ko) | 1991-05-28 |
Family
ID=17648778
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1019880014771A KR910003342B1 (ko) | 1987-11-10 | 1988-11-10 | 활성탄의 제조방법 |
Country Status (8)
Country | Link |
---|---|
US (1) | US4921831A (ko) |
EP (1) | EP0315842B1 (ko) |
JP (1) | JPH01126214A (ko) |
KR (1) | KR910003342B1 (ko) |
CN (1) | CN1010765B (ko) |
AU (1) | AU588752B2 (ko) |
CA (1) | CA1321782C (ko) |
DE (1) | DE3880438T2 (ko) |
Families Citing this family (39)
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US5063070A (en) * | 1989-06-30 | 1991-11-05 | Nabisco Brands, Inc. | Processes for separation of sterol compounds from fluid mixtures using substantially insoluble compounds |
US5091117A (en) * | 1990-04-16 | 1992-02-25 | Nabisco Brands, Inc. | Process for the removal of sterol compounds and saturated fatty acids |
US5187141A (en) * | 1990-08-24 | 1993-02-16 | Jha Mahesh C | Process for the manufacture of activated carbon from coal by mild gasification and hydrogenation |
DE4132971C2 (de) * | 1991-10-04 | 1996-02-01 | Bergwerksverband Gmbh | Verfahren zur Herstellung von Kohlenstoffmolekularsieben |
US5248413A (en) * | 1992-02-28 | 1993-09-28 | University Of Kentucky Research Foundation | Process for removing sulfur and producing enhanced quality and environmentally acceptable products for energy production from coal |
US5254521A (en) * | 1992-08-03 | 1993-10-19 | University Of North Dakota Energy And Environment Research Center Foundation | Leonardite char adsorbents |
US5405593A (en) * | 1992-08-03 | 1995-04-11 | University Of North Dakota Energy And Environmental Research Center Foundation | Leonardite char adsorbents |
JPH08158248A (ja) * | 1994-12-03 | 1996-06-18 | Kensho Muramoto | クリーニング用活性炭及びクリーニング方法並びに活性炭の再処理装置 |
US5965479A (en) * | 1995-02-03 | 1999-10-12 | Mitsubishi Chemical Corporation | Activated carbon and process for producing the same |
JPH0986913A (ja) * | 1995-09-26 | 1997-03-31 | Mitsubishi Chem Corp | 活性炭およびその製造方法 |
US5905629A (en) * | 1995-09-28 | 1999-05-18 | Westvaco Corporation | High energy density double layer energy storage devices |
US5926361A (en) * | 1995-09-28 | 1999-07-20 | Westvaco Corporation | High power density double layer energy storage devices |
US6060424A (en) * | 1995-09-28 | 2000-05-09 | Westvaco Corporation | High energy density carbons for use in double layer energy storage devices |
US6043183A (en) * | 1995-09-28 | 2000-03-28 | Westvaco Corporation | High power density carbons for use in double layer energy storage devices |
US5990041A (en) * | 1996-04-05 | 1999-11-23 | Research Foundation Of State University Of New York At Buffalo | Mesoporous activated carbon filaments |
CN1057745C (zh) * | 1997-06-25 | 2000-10-25 | 宁夏万得活性炭有限公司 | 一种用无烟煤制造的不定型颗粒活性炭及其制造方法 |
WO1999008777A1 (en) | 1997-08-19 | 1999-02-25 | Electric Power Research Institute, Inc. | Apparatus and method for removal of vapor phase contaminants from a gas stream by in-situ activation of carbon-based sorbents |
US6558454B1 (en) | 1997-08-19 | 2003-05-06 | Electric Power Research Institute, Inc. | Method for removal of vapor phase contaminants from a gas stream by in-situ activation of carbon-based sorbents |
US5795854A (en) * | 1997-11-20 | 1998-08-18 | The Procter & Gamble Company | Detergent composition containing cylindrically-shaped bleach activator extrudates |
JP4143150B2 (ja) * | 1997-11-25 | 2008-09-03 | 株式会社キャタラー | 活性炭の製造方法 |
DE50012022D1 (de) * | 2000-05-24 | 2006-03-30 | Carbotex Produktions Und Vered | Verfahren zur herstellung von geformter aktivkohle |
CA2367818C (en) | 2001-01-18 | 2010-05-11 | Electric Power Research Institute, Inc. | Method and apparatus for renewable mercury sorption |
CA2381610C (en) | 2001-04-16 | 2010-07-06 | Electric Power Research Institute, Inc. | Method and apparatus for removing vapor phase contaminants from a flue gas stream |
US6905534B2 (en) * | 2001-04-16 | 2005-06-14 | Electric Power Research Institute, Inc. | Method and apparatus for removing vapor phase contaminants from a flue gas stream |
JP4708409B2 (ja) * | 2001-07-26 | 2011-06-22 | クラレケミカル株式会社 | 廃ガス処理用成型活性炭及びその製造方法 |
US20080063592A1 (en) * | 2004-05-20 | 2008-03-13 | Kuraray Chemical Co., Ltd | Spherical Active Carbon And Process For Producing The Same |
US20060107589A1 (en) | 2004-11-19 | 2006-05-25 | Rubin Patti D | Compressed growing medium |
US9756798B2 (en) | 2004-11-19 | 2017-09-12 | Patti D. Rubin | Burrow filling compressed growing medium |
US7407121B2 (en) * | 2004-12-28 | 2008-08-05 | Kerns Kevin C | Method and process for providing a controlled batch of micrometer-sized or nanometer-sized coal material |
US20060154815A1 (en) * | 2005-01-12 | 2006-07-13 | Kuraray Chemical Co., Ltd. | Pelletized activated carbon and production method for the same |
WO2009058869A1 (en) | 2007-10-29 | 2009-05-07 | Oms Investments, Inc. | Compressed coconut coir pith granules and methods for the production and use thereof |
CN101817524A (zh) * | 2010-05-05 | 2010-09-01 | 卞奎友 | 一种利用物理活化法生产活性炭的工艺 |
US20160229697A1 (en) * | 2015-02-05 | 2016-08-11 | Advanced Organic Methods LLC | Activated Carbon Production at Biomass-Fueled Steam/Electric Power Plants |
CN105800610B (zh) | 2016-03-31 | 2018-03-27 | 神华集团有限责任公司 | 一种无粘结剂煤基压块活性炭的制备方法 |
CN106315547A (zh) * | 2016-07-28 | 2017-01-11 | 中山大学 | 一种多孔炭材料及其制备方法和应用 |
WO2019161077A1 (en) | 2018-02-15 | 2019-08-22 | Praxair Technology, Inc. | Superior core-in-shell component composite adsorbents for vsa/vpsa/psa systems |
US10941042B2 (en) * | 2018-04-06 | 2021-03-09 | West Virginia University | Processes and compositions for carbon foams and materials |
US11858818B2 (en) | 2019-10-24 | 2024-01-02 | West Virginia University | Processes and compositions for carbon foam materials |
CN112239206B (zh) * | 2020-11-11 | 2021-05-28 | 江苏浦士达环保科技股份有限公司 | 一种低灰压块煤质活性炭制备方法 |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2648637A (en) * | 1948-08-06 | 1953-08-11 | Rodman Chemical Company | Method of producing activated carbon |
DE1800238B2 (de) * | 1968-10-01 | 1974-09-26 | Bergwerksverband Gmbh, 4300 Essen | Verfahren zur Herstellung von Formkoksen in Kugelform |
US4032487A (en) * | 1974-03-21 | 1977-06-28 | Borden, Inc. | Aqueous acrylate-epoxy silane crosslinker adhesive dispersion composition |
US4268417A (en) * | 1977-09-26 | 1981-05-19 | American Minechem Corporation | Method of making activated carbon |
AU6226480A (en) * | 1979-08-01 | 1981-03-03 | Carborundum Company, The | Hard granular activated carbon manufactured from sub- bituminous cola treated with dilute solution of saturated aliphatic monocarboxylic acid |
AU6227280A (en) * | 1979-08-01 | 1981-03-03 | Carborundum Company, The | Hard granular activated carbon manufactured from sub- bituminous coal treated with solid boric acid |
US4410472A (en) * | 1982-01-15 | 1983-10-18 | Aluminum Company Of America | Method for making spherical binderless pellets |
SU1263623A1 (ru) * | 1982-08-11 | 1986-10-15 | Институт горючих ископаемых | Способ получени гранулированного активированного угл |
-
1987
- 1987-11-10 JP JP62282152A patent/JPH01126214A/ja active Granted
-
1988
- 1988-10-19 US US07/259,592 patent/US4921831A/en not_active Expired - Fee Related
- 1988-10-28 DE DE88118024T patent/DE3880438T2/de not_active Expired - Fee Related
- 1988-10-28 EP EP88118024A patent/EP0315842B1/en not_active Expired - Lifetime
- 1988-10-31 CA CA000581734A patent/CA1321782C/en not_active Expired - Fee Related
- 1988-11-02 AU AU24626/88A patent/AU588752B2/en not_active Ceased
- 1988-11-08 CN CN85107024A patent/CN1010765B/zh not_active Expired
- 1988-11-10 KR KR1019880014771A patent/KR910003342B1/ko not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
JPH01126214A (ja) | 1989-05-18 |
EP0315842A2 (en) | 1989-05-17 |
JPH0516371B2 (ko) | 1993-03-04 |
EP0315842B1 (en) | 1993-04-21 |
CN1010765B (zh) | 1990-12-12 |
EP0315842A3 (en) | 1990-09-19 |
DE3880438D1 (de) | 1993-05-27 |
KR910003342B1 (ko) | 1991-05-28 |
AU588752B2 (en) | 1989-09-21 |
US4921831A (en) | 1990-05-01 |
DE3880438T2 (de) | 1993-11-25 |
CA1321782C (en) | 1993-08-31 |
AU2462688A (en) | 1989-05-25 |
CN1033262A (zh) | 1989-06-07 |
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