|Publication number||US5185307 A|
|Application number||US 07/741,512|
|Publication date||Feb 9, 1993|
|Filing date||Feb 9, 1990|
|Priority date||Feb 10, 1989|
|Also published as||DE69004567D1, EP0458839A1, EP0458839B1, WO1990009235A1|
|Publication number||07741512, 741512, PCT/1990/88, PCT/SE/1990/000088, PCT/SE/1990/00088, PCT/SE/90/000088, PCT/SE/90/00088, PCT/SE1990/000088, PCT/SE1990/00088, PCT/SE1990000088, PCT/SE199000088, PCT/SE90/000088, PCT/SE90/00088, PCT/SE90000088, PCT/SE9000088, US 5185307 A, US 5185307A, US-A-5185307, US5185307 A, US5185307A|
|Inventors||Ulf Hakansson, Lars Falth|
|Original Assignee||Ulf Hakansson, Faelth Lars|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (5), Referenced by (4), Classifications (8), Legal Events (3)|
|External Links: USPTO, USPTO Assignment, Espacenet|
History of the Related Art
The discharge of organic substances from industrial processes to the surroundings has become a serious environmental threat and methods for reducing such discharges have become more and more important. For a long time, it has been known that with the aid of certain sorbtion agents a considerable part of the contaminants in question can be trapped and subsequently rendered harmless or recovered.
Lately, interest has been focused on a group of inorganic substances, so-called zeolites as sorbtion agents, primarily since it has been possible to give them selectivity in sorbtion capacity with respect to the gaseous constituents in the contaminating agent, a selectivity which to a great degree excludes sorbtion of water vapor in spite of the fact that the injurious contaminants are separated with high efficiency. An example of how such a so-called hydrophobic zeolite can be built up is given in the Swedish Patent No. 8604873-3.
The hydrophobic zeolites eliminate a large problem with previously used sorbtion agents in the often recurring operational cases where the contaminating agent contains water vapour. The sorbtion capacity of the sorbtion agent has in such cases been appropriated to a large degree by the water vapor, reducing to a corresponding degree the sorbtion capacity for the injurious part of the contaminant. In turn, this has lead to lowered capacity of the sorbtion plant and furthermore to heavily increased operational costs for regenerating the sorbtion agent. The less tendency for water vapor sorbtion by the hydrophobic zeolites which could be provided, the more effective and operationally cheap the purification process has become.
An effective utilization of the sorbtion capacity of the hydrophobic zeolites requires, inter alia, that they are exposed in a fixed geometric structure in the contaminating agent, this structure permitting an intimate contact between zeolite and the flowing medium while at the same time permitting a large medium flow without a too high pressure drop. Such structures in the form of cellular bodies having alternatingly flat and pleated thin layers, which are caused to support each other at mutually separated places so that throughducts or gaps are formed have long been successfully used, e.g. for drying air.
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 the layer so that it is given high mechanical strength. This cellular body is described in the Swedish Patent No. 8003175-0. Among the powders used has been the type of zeolite intended for absorbing moisture from air, and as a binder the precipitate occurring when waterglass is exposed to such as carbon dioxide or calcium chloride.
It has been apparently obvious to apply the same technique for achieving a cellular body for the hydrophobic zeolites, but in practice it has not been found possible to achieve acceptable results in this way. The binding agents which have been suggested have namely had hygroscopic properties, which is not a disadvantage when it is a question of bodies intended for the removal of moisture. In such a case, the hygroscopic capacity has even been desirable. However, when it is a question of fixing the hydrophobic zeolites in the cell structure, there is the requirement that the finished cellular body does not contain any hygroscopic components which would reduce the effect of the hydrophobic properties of the zeolites.
It is the object of this invention to form a cellular body of the kind described, where the hydrophobic zeolites are bonded in the layers with non-hygroscopic binders while the layers are given a great degree of mechanical stiffness. It is also one of the objects of the invention to provide this without the binder substantially blocking access to the pores of the zeolites for the contaminants which are to be absorbed, or affect the pore structure of the zeolite so that the hydrophobic properties are deteriorated.
In addition, it is an object to achieve a cellular body of exclusively inorganic, non-inflammable constituents so that the body can be regenerated at a high air temperature.
These objects are achieved by the cell structure in accordance with the invention being impregnated with a sludge of the hydrophobic zeolite and an inorganic binder, after which the impregnated cellular structure is heated to a temperature at which sintering between the constituents begins to occur and the cellular body is given sufficient strength.
The starting material for the cellular structure is preferably layers of inorganic artificial fibres, impregnation taking place by the produced structure being doused or dipped in the sludge of zeolite and binder. For getting the desired amount of the sludge into the cellular structure, 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 favorable 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 properties of the zeolite being negatively affected.
As mentioned, the cellular body is impregnated with a sludge of zeolites and binder, and the mixing ratio between binder and zeolite is preferably between 0.05 and 1.00 based on dry weights, the range 0.10 to 0.35 having been found to be particularly suitable. The mixing ratio should 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.
After impregnation by the sludge, optionally in several steps with intermediate drying, 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 which any ability of the binder to absorb water is succesively reduced, e.g. at least 500°-600° C. During the heat treatment, the organic substances or binder which 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 accordance with the method described in the introduction.
An aqueous sludge of zeolites and clay in a mixing ratio 12% zeolite, 4% clay and 84% water, giving a dry substance of 16% was used. Treatment of the cellular body was carried out by dipping twice with intermediate 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 hydrophobicity.
With the aid of the described production of a cellular body by impregnation with a sludge of a hydrophobic zeolite and an inorganic binder together with heating to a temperature at which sintering takes place, there is provided a cellular body which is extremely well-suited to adsorbtion of organic substances, such as solvents from the air in industrial discharges.
The invention is naturally not limited to the described example but can be varied within the scope of the following Claims.
Accordingly, 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 contaminants of an organic nature. The binder used can also be more or less hydrophobic before heat treatment, but where possible water vapor sorbtion capacity of the binder is present, this will be reduced by the heat treatment.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US4420419 *||Mar 8, 1982||Dec 13, 1983||Mizusawa Kagaku Kogyo Kabushiki Kaisha||Abrasion-resistant granular zeolite and process for preparation thereof|
|US4608361 *||Dec 8, 1983||Aug 26, 1986||Nichias Corporation||Catalyst carriers and process for preparation of the same|
|US4886769 *||Jun 10, 1988||Dec 12, 1989||Kabushiki Kaisha Seibu Giken||Active gas adsorbing element and method of manufacturing|
|JPS4725998A *||Title not available|
|JPS49105786A *||Title not available|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US7094390||May 13, 2005||Aug 22, 2006||Exxonmobil Chemical Patents Inc.||Macrostructures of porous inorganic material and process for their preparation|
|US7378076||Aug 11, 2005||May 27, 2008||Exxonmobil Chemical Patents Inc.||Process for production of macrostructures of a microporous material|
|US20050209092 *||May 13, 2005||Sep 22, 2005||Sterte Per J||Macrostructures of porous inorganic material and process for their preparation|
|US20050266984 *||Aug 11, 2005||Dec 1, 2005||Sterte Per J||Process for production of macrostructures of a microporous material|
|U.S. Classification||502/68, 502/527.2, 502/60|
|International Classification||C01B39/02, C01B39/00, B01J20/18|
|Aug 2, 1996||FPAY||Fee payment|
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|Jul 12, 2000||FPAY||Fee payment|
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|Jul 28, 2004||FPAY||Fee payment|
Year of fee payment: 12