WO1990009235A1 - Method for producing a cellular body - Google Patents
Method for producing a cellular body Download PDFInfo
- Publication number
- WO1990009235A1 WO1990009235A1 PCT/SE1990/000088 SE9000088W WO9009235A1 WO 1990009235 A1 WO1990009235 A1 WO 1990009235A1 SE 9000088 W SE9000088 W SE 9000088W WO 9009235 A1 WO9009235 A1 WO 9009235A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- binder
- cellular
- cellular body
- sludge
- zeolite
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/16—Alumino-silicates
- B01J20/18—Synthetic zeolitic molecular sieves
- B01J20/183—Physical conditioning without chemical treatment, e.g. drying, granulating, coating, irradiation
Definitions
- ⁇ e hy ⁇ rophobic zeolites eliminate a large problem with previously used sorbtion agents in the often recurring operational cases where the cxxrtaminating agent contains water vapour.
- the sorbtion capacity of the sorbtion agent has in such cases been appropriated to a large degree by the water vapour, reducing to a corresponding degree the sorbtion capacity for the injurious part of tfte containinant. m turn, this has lead to lowered capacity of the sorbtion plant and furthermore to heavily increased operational costs for regenerating the sorbtion agent. Ihe less teridency for water vapour sorbtion by the hydrophobic zeolites which could be provided, the more effective and operationally cheap the purification process has become.
- a particularly advantageous embodiment is one where the starting material is a paper built up of sparcely layered mineral fibres, preferably glass fibres, which after building up the cellular structure are supplied with powder and binder filling out the gaps between the fibres and thereby sealing the layer simultaneously as the powder and binder combine to stiffen up the layer so that it is given high mechanical strength.
- This cellular body is described in the Swedish Patent No. 8003175-0.
- the powders used has been the type of zeolite intended for absorbing moisture from air, and as a binder the precipitate ccx-urring when waterglass is exposed to such as carbon dioxide or calcium chloride.
- the starting material for the cellular structure is preferably layers of iriorganic artificial fibres, impregnation taking , place by the produced structure being doused or dipped in the sludge of zeolite and binder.
- impregnation optionally takes place in several steps and the cellular body is heated between the steps for drying out water vapour.
- Zeolites which have a high hydrophobic capacity e.g. de-aluminized zeolite, are used as an active substance or adsorbent.
- the inorganic binder includes clay. Particularly favourable results have been obtained with a sludge of kaolin-type clay of an alkaline nature or with alkaline additives to the sludge. In such a case, the pH value should be as high as possible without the hydrophobic pro ⁇ perties of the zeolite being negatively affected.
- the mixing ratio shall be as low as possible, inter alia so that the binder will not block access to the pores of the zeolite, but primarily for maximizing the amount of zeolite in the cellular body.
- the cellular body is fired at a temperature causing sintering together of the constituents in the impregnated cellular structure and preferably at a temperature at whicli any ability of the binder to absorb water is successively redu»d, e.g. at least 500-600 ⁇ C.
- the organic substances or binder which can have been in the cell structure from the beginning are also fired away.
- Paper made from inorganic artificial fibres is used for the production of a cellular body which is formed to a cellular structure in accor ⁇ dance with the method described in the introduction.
- Treat ⁇ ment of the cellular body was carried out by dipping twice with irrtermediate drying, a final firing being carried out at 600 ⁇ C. This treatment gave a cellular body with a zeolite content of 60% by weight, good strength and excellent hdrophobi ⁇ ity.
- the cellular body although it has been described for purifying gas such as air, can also be used for purifying other media such as liquids, e.g. water from ⁇ ntaminants of an organic nature.
- the binder used can also be more or less hydrophobic before heat treatment, but where possible water vapour sorbtion capacity of the binder is present, this shall be reduced by the heat treatment.
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE8900469A SE466533B (en) | 1989-02-10 | 1989-02-10 | PROCEDURES FOR PREPARING CELL CELLS |
SE8900469-1 | 1989-02-10 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1990009235A1 true WO1990009235A1 (en) | 1990-08-23 |
Family
ID=20375010
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/SE1990/000088 WO1990009235A1 (en) | 1989-02-10 | 1990-02-09 | Method for producing a cellular body |
Country Status (7)
Country | Link |
---|---|
US (1) | US5185307A (en) |
EP (1) | EP0458839B1 (en) |
JP (1) | JPH04503326A (en) |
AU (1) | AU5081190A (en) |
DE (1) | DE69004567D1 (en) |
SE (1) | SE466533B (en) |
WO (1) | WO1990009235A1 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0516949A1 (en) * | 1991-05-27 | 1992-12-09 | Degussa Aktiengesellschaft | Molded bodies containing dealuminized zeolite Y and process for manufacturing them |
WO1995005239A1 (en) * | 1993-08-14 | 1995-02-23 | Wilhelm Söndgen Gmbh | Filters for water or aqueous solutions and associated filtering process |
US6171568B1 (en) * | 1991-05-27 | 2001-01-09 | Degussa-H{umlaut over (u)}ls Aktiengesellschaft | Method for the purification of exhaust air and/or effluents by contact with moulded bodies containing dealuminated zeolite Y |
EP1190766A1 (en) * | 2000-09-26 | 2002-03-27 | Nichias Co., Ltd. | Slurry for carrying zeolite and method for manufacturing zeolite-carrying adsorption element |
US6569400B1 (en) | 1998-06-29 | 2003-05-27 | Exxon Mobil Chemical Patents Inc. | Process for production of macrostructures of a microporous material |
US6908604B2 (en) | 1999-05-17 | 2005-06-21 | Exxonmobil Chemical Patents Inc. | Macrostructures of porous inorganic material and process for their preparation |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0057416A1 (en) * | 1981-02-03 | 1982-08-11 | Battelle-Institut e.V. | Zeolitic molecular sieve and process for producing it |
EP0068816A1 (en) * | 1981-06-23 | 1983-01-05 | Takeda Chemical Industries, Ltd. | Multilayer glazing structure |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5322552B2 (en) * | 1973-02-12 | 1978-07-10 | ||
JPS5915028B2 (en) * | 1980-03-26 | 1984-04-07 | ニチアス株式会社 | Manufacturing method of catalyst carrier |
JPS6025369B2 (en) * | 1981-03-10 | 1985-06-18 | 水澤化学工業株式会社 | Wear-resistant granular zeolite and its manufacturing method |
JP2579767B2 (en) * | 1987-06-10 | 1997-02-12 | 株式会社 西部技研 | Ultra-low concentration gas adsorption element and gas adsorption removal device |
-
1989
- 1989-02-10 SE SE8900469A patent/SE466533B/en unknown
-
1990
- 1990-02-09 WO PCT/SE1990/000088 patent/WO1990009235A1/en active IP Right Grant
- 1990-02-09 DE DE90903236T patent/DE69004567D1/en not_active Expired - Lifetime
- 1990-02-09 US US07/741,512 patent/US5185307A/en not_active Expired - Lifetime
- 1990-02-09 JP JP2503384A patent/JPH04503326A/en active Pending
- 1990-02-09 AU AU50811/90A patent/AU5081190A/en not_active Abandoned
- 1990-02-09 EP EP90903236A patent/EP0458839B1/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0057416A1 (en) * | 1981-02-03 | 1982-08-11 | Battelle-Institut e.V. | Zeolitic molecular sieve and process for producing it |
EP0068816A1 (en) * | 1981-06-23 | 1983-01-05 | Takeda Chemical Industries, Ltd. | Multilayer glazing structure |
Non-Patent Citations (1)
Title |
---|
PATENT ABSTRACTS OF JAPAN, Vol. 8, No 232, C248, Abstract of JP 59-115740, publ 1984-07-04 (MITSUBISHI JUKOGYO K.K.). * |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0516949A1 (en) * | 1991-05-27 | 1992-12-09 | Degussa Aktiengesellschaft | Molded bodies containing dealuminized zeolite Y and process for manufacturing them |
US5316993A (en) * | 1991-05-27 | 1994-05-31 | Degussa Aktiengesellschaft | Molded bodies containing dealuminated zeolite Y and the process for their production |
US6171568B1 (en) * | 1991-05-27 | 2001-01-09 | Degussa-H{umlaut over (u)}ls Aktiengesellschaft | Method for the purification of exhaust air and/or effluents by contact with moulded bodies containing dealuminated zeolite Y |
WO1995005239A1 (en) * | 1993-08-14 | 1995-02-23 | Wilhelm Söndgen Gmbh | Filters for water or aqueous solutions and associated filtering process |
US6569400B1 (en) | 1998-06-29 | 2003-05-27 | Exxon Mobil Chemical Patents Inc. | Process for production of macrostructures of a microporous material |
US6949239B2 (en) | 1998-06-29 | 2005-09-27 | Exxonmobil Chemical Patents Inc. | Process for production of macrostructures of a microporous material |
US7378076B2 (en) | 1998-06-29 | 2008-05-27 | Exxonmobil Chemical Patents Inc. | Process for production of macrostructures of a microporous material |
US6908604B2 (en) | 1999-05-17 | 2005-06-21 | Exxonmobil Chemical Patents Inc. | Macrostructures of porous inorganic material and process for their preparation |
EP1190766A1 (en) * | 2000-09-26 | 2002-03-27 | Nichias Co., Ltd. | Slurry for carrying zeolite and method for manufacturing zeolite-carrying adsorption element |
KR100805508B1 (en) * | 2000-09-26 | 2008-02-20 | 니찌아스 카부시키카이샤 | Slurry for carrying zeolite and method for manufacturing zeolite-carrying adsorption element |
Also Published As
Publication number | Publication date |
---|---|
SE8900469L (en) | 1990-08-11 |
JPH04503326A (en) | 1992-06-18 |
EP0458839B1 (en) | 1993-11-10 |
SE466533B (en) | 1992-03-02 |
SE8900469D0 (en) | 1989-02-10 |
AU5081190A (en) | 1990-09-05 |
DE69004567D1 (en) | 1993-12-16 |
EP0458839A1 (en) | 1991-12-04 |
US5185307A (en) | 1993-02-09 |
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