WO1989008500A1 - Composite adsorbents - Google Patents

Composite adsorbents

Info

Publication number
WO1989008500A1
WO1989008500A1 PCT/GB1989/000245 GB8900245W WO8908500A1 WO 1989008500 A1 WO1989008500 A1 WO 1989008500A1 GB 8900245 W GB8900245 W GB 8900245W WO 8908500 A1 WO8908500 A1 WO 8908500A1
Authority
WO
WIPO (PCT)
Prior art keywords
gel
organic polymer
solution
polymer
inorganic
Prior art date
Application number
PCT/GB1989/000245
Other languages
French (fr)
Inventor
Eric Robinson
Original Assignee
Eric Robinson
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Eric Robinson filed Critical Eric Robinson
Publication of WO1989008500A1 publication Critical patent/WO1989008500A1/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
    • B01J20/28047Gels
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/06Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
    • B01J20/08Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04 comprising aluminium oxide or hydroxide; comprising bauxite
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/10Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/103Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate comprising silica
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26Synthetic macromolecular compounds
    • B01J20/261Synthetic macromolecular compounds obtained by reactions only involving carbon to carbon unsaturated bonds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26Synthetic macromolecular compounds
    • B01J20/262Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon to carbon unsaturated bonds, e.g. obtained by polycondensation

Definitions

  • the present invention relates to compositions of matter for use as adsorbents or ion exchange materials.
  • Natural polymers such as chitosan, starch and alginic acid are useful adsorbents and ion exchangers in that they possess hydroxyl, amino or carboxyl groups which are all useful sites for adsorption or exchange.
  • the accessibility to these sites is generally poor because the compact structure of the polymer prevents diffusion of large ions.
  • Porous inorganic materials such as silica gel and silica alumina possess high surface areas and additionally have a form and mechanical strength appropriate to industrial use, but lack the adsorptive capacity of many polymers.
  • Organic polymers have been coated onto solid supports to improve their mechanical strength and accessible surface area.
  • chitosan has been coated onto diatomaceous earth for effluent treatment processes.
  • the object of the present invention is to provide improved adsorbent materials which possess good mechanical strength, good accessibility to adsorption sites and high adsorptive capacity.
  • an adsorbent material comprising an inorganic gel and an organic polymer, wherein the polymer is uniformly and intimately distributed throughout the inorganic gel.
  • the present invention also provides a process for preparing a composition as defined in accordance with the invention, which process comprises forming an unstable inorganic sol which has dissolved therein an organic polymer, mixing vigorously and allowing or causing the unstable inorganic sol to gel entrapping the polymer therein.
  • Formation of an unstable sol is conveniently accomplished by adding an acid such as sulphuric, nitric, hydrochloric, acetic or formic acid to a suitable precursor such as sodium silicate or in the case of silica alumina adding a solution of sodium aluminate to a solution of sodium silicate.
  • the unstable sol may be formed by taking a freshly prepared gel and by vigorous mechanical action reducing this to colloidal dimensions.
  • organic polymers for use with the invention include starch, dextran, chitosan, carboxymethyl cellulose, sodium carboxymethyl cellulose, polyvinyl alcohol, agar, agarose, carrageenan, gelatin, sodium alginate or albumin.
  • the organic polymer is added prior to the conversion of the inorganic sol into a gel, the addition being made at a point where the pH is appropriate to avoid precipitation of the polymer.
  • the polymer may be mixed with a precursor of the sol, such as sodium silicate or sodium aluminate, or with the sol itself.
  • Organic polymers or salts of polymers which are soluble in alkaline solution such as starch or sodium alginate may be added conveniently to a precursar of the sol, whereas other polymers which are only soluble under neutral or acidic conditions are added to the unstable inorganic sol prior to gelation.
  • the composition contains between 5 and 50% by weight of the organic polymer.
  • the composition is allowed to age for between 2 and 48 hours before being broken and washed. During this time the strength of the inorganic gel increases.
  • the material may be used without drying but a stronger product is obtained if it is dried before use. Drying is conveniently undertaken by heating between 50 and 100°C for example at 80°C.
  • a solution of sodium silicate is added to a solution of sulphuric acid such that the pH is in the range 5 to 7 after the addition.
  • a solution of a polymer soluble under acidic conditions such as a solution of chitosan in formic acid is added with vigorous stirring.
  • the intimate mixture is then allowed to gel to a continuous mass. This is aged for a period of up to 48 hours after which it is broken through a sieve into water, washed and dried.
  • a solution of a polymer soluble in alkali such as a solution of starch is added to a solution of sodium silicate and thoroughly mixed.
  • a solution of sodium aluminate is then added with stirring and the intimate mixture is allowed to gel to a continuous mass.
  • the gel is aged for up to 48 hours after which it is broken through a sieve, washed and dried.
  • the particle size of the material after drying may be conveniently controlled by selection of the dimensions of the sieve through which the wet gel is broken.
  • a particular benefit of the material according to the present invention is that a polymer which is normally soluble in water may be held in an insoluble state in an aqueous environment.
  • sodium carboxymethyl cellulose may be used for water treatment since when combined intimately with for example silica gel according to the present invention it is held within the rigid structure of the inorganic gel such that little leaching occurs with time.
  • the organic polymer may be cross-linked within the structure by for example treatment with a solution of formaldehyde or glutaraldehyde, though such treatment will reduce the adsorptive capacity.
  • compositions according to the invention have application in liquid effluent treatment, for the removal of heavy metals and other toxic materials, in the treatment of potable water, in separation processes and ion exchange, and in biocatalyst and heterogeneous catalyst support.
  • Example 5 A column 2.5 cm in diameter and 56' cm long was packed with the material of Example 5 and a solution containing 10 milligram/litre of lead was was passed through the material at 15°C. The effluent from the column was analysed and found to contain less than 1 microgram/litre of lead. Similar results were obtained for aluminium.
  • Example 5 A sample of the material prepared in Example 5 was placed in a 1% solution of copper nitrate at 15°C. The solution was analysed before and after equilibrium adsorption. The adsorption capacity for copper was 160 g Cu per g chitosan. Using an acidified solution of copper sulphate the adsorption capacity was similarly measured at 175 mg Cu per gram chitosan.
  • Example 8 A sample of the material of Example 8 was placed in a 1% solution of copper sulphate and the solution analysed before and after equilibrium adsorption. The adsorption capacity for copper was found to be 187 mg/g polymer.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

An adsorbent material comprises a composite of an inorganic gel such as silica gel and an organic polymer such as chitosan, the polymer being uniformly distributed throughout the gel. As part of the composite, a polymer placed in an environment in which it is normally soluble may be held in an insoluble state, and used for adsorption of pollutants from effluent or potable water.

Description

COMPOSITE ADSORBENTS
The present invention relates to compositions of matter for use as adsorbents or ion exchange materials.
Natural polymers such as chitosan, starch and alginic acid are useful adsorbents and ion exchangers in that they possess hydroxyl, amino or carboxyl groups which are all useful sites for adsorption or exchange. However the accessibility to these sites is generally poor because the compact structure of the polymer prevents diffusion of large ions. In addition they lack mechanical strength and appropriate form for use in industrial processes. Porous inorganic materials such as silica gel and silica alumina possess high surface areas and additionally have a form and mechanical strength appropriate to industrial use, but lack the adsorptive capacity of many polymers.
Organic polymers have been coated onto solid supports to improve their mechanical strength and accessible surface area. For example chitosan has been coated onto diatomaceous earth for effluent treatment processes.
However such coating processes do not make use of a large proportion of the available surface area of the porous support because the polymer solution, by virtue of viscosity, cannot penetrate the fine pores of the support.
The object of the present invention is to provide improved adsorbent materials which possess good mechanical strength, good accessibility to adsorption sites and high adsorptive capacity.
According to the present invention there is provided an adsorbent material comprising an inorganic gel and an organic polymer, wherein the polymer is uniformly and intimately distributed throughout the inorganic gel. The present invention also provides a process for preparing a composition as defined in accordance with the invention, which process comprises forming an unstable inorganic sol which has dissolved therein an organic polymer, mixing vigorously and allowing or causing the unstable inorganic sol to gel entrapping the polymer therein.
Examples of inorganic gels for use in the present invention include silica gel, silica alumina gel or alumina gel. Formation of an unstable sol is conveniently accomplished by adding an acid such as sulphuric, nitric, hydrochloric, acetic or formic acid to a suitable precursor such as sodium silicate or in the case of silica alumina adding a solution of sodium aluminate to a solution of sodium silicate. Alternatively the unstable sol may be formed by taking a freshly prepared gel and by vigorous mechanical action reducing this to colloidal dimensions.
Examples of organic polymers for use with the invention include starch, dextran, chitosan, carboxymethyl cellulose, sodium carboxymethyl cellulose, polyvinyl alcohol, agar, agarose, carrageenan, gelatin, sodium alginate or albumin.
The organic polymer is added prior to the conversion of the inorganic sol into a gel, the addition being made at a point where the pH is appropriate to avoid precipitation of the polymer. Thus the polymer may be mixed with a precursor of the sol, such as sodium silicate or sodium aluminate, or with the sol itself. Organic polymers or salts of polymers which are soluble in alkaline solution such as starch or sodium alginate may be added conveniently to a precursar of the sol, whereas other polymers which are only soluble under neutral or acidic conditions are added to the unstable inorganic sol prior to gelation.
It is preferred that the composition contains between 5 and 50% by weight of the organic polymer. Preferably the composition is allowed to age for between 2 and 48 hours before being broken and washed. During this time the strength of the inorganic gel increases. The material may be used without drying but a stronger product is obtained if it is dried before use. Drying is conveniently undertaken by heating between 50 and 100°C for example at 80°C.
In a first embodiment of the invention a solution of sodium silicate is added to a solution of sulphuric acid such that the pH is in the range 5 to 7 after the addition. Before the sol thus formed gels, a solution of a polymer soluble under acidic conditions, such as a solution of chitosan in formic acid is added with vigorous stirring. The intimate mixture is then allowed to gel to a continuous mass. This is aged for a period of up to 48 hours after which it is broken through a sieve into water, washed and dried.
In a second embodiment of the invention a solution of a polymer soluble in alkali such as a solution of starch is added to a solution of sodium silicate and thoroughly mixed. A solution of sodium aluminate is then added with stirring and the intimate mixture is allowed to gel to a continuous mass. The gel is aged for up to 48 hours after which it is broken through a sieve, washed and dried.
The particle size of the material after drying may be conveniently controlled by selection of the dimensions of the sieve through which the wet gel is broken.
During the course of work on the present invention I have found that when the material of the invention is treated with a solution of ammonium hydroxide before or after drying the adsorption capacity towards metal ions in solution is considerably increased.
A particular benefit of the material according to the present invention is that a polymer which is normally soluble in water may be held in an insoluble state in an aqueous environment. Thus, for example, sodium carboxymethyl cellulose may be used for water treatment since when combined intimately with for example silica gel according to the present invention it is held within the rigid structure of the inorganic gel such that little leaching occurs with time. Where the material must be used in an aggressive environment, for example at elevated temperatures, the organic polymer may be cross-linked within the structure by for example treatment with a solution of formaldehyde or glutaraldehyde, though such treatment will reduce the adsorptive capacity.
Compositions according to the invention have application in liquid effluent treatment, for the removal of heavy metals and other toxic materials, in the treatment of potable water, in separation processes and ion exchange, and in biocatalyst and heterogeneous catalyst support.
The invention will be further apparent from the following examples :-
EXAMPLE 1
To a solution of formic acid (20 ml formic acid in 200 ml water) was added slowly with stirring, 200 ml of 50% commercial sodium silicate (29.9% Si02) . To this was added 100 ml of a solution of 4% chitosan in water containing 4 ml formic acid, the addition being completed within 3 minutes. The mixture was stirred vigorously for 2 minutes then allowed to stand while a gel formed. After 24 hours the gel was broken, washed and dried to yield 60 g of a composite which had a pore volume of 0.36 ml/ml, or 0.32 ml/g, a density of 1.14 g/cm3, a surface area of 150 m2/g, and a high adsorption capacity for dyes and organics such as phenol. EXAMPLE 2
20 g of starch was dissolved in 200 ml of boiling water and the solution was cooled. This was added to a stirred solution of 36 ml of sodium silicate in 100 ml water. Stirring was continued while 3.9 ml cone, sulphuric acid in 100 ml water was added. After 1 minute stirring was discontinued and a gel formed which was aged for 24 hours before being broken, washed and dried. Microscopic examination of the material stained with iodine showed that the composite gel was homogeneous. The material actively removed metal ions such as copper and chromium from solution.
EXAMPLE 3
10 g of starch was dissolved in 100 ml boiling water and the solution was cooled. This was added to a solution of 36 ml sodium silicate in 200 ml of water and the solution was stirred while 16.4 g of sodium aluminate in 200 ml water was added. Stirring was stopped to allow gelation and the cogel was aged for 12 hours. The gel was then broken, washed and dried. This composite could be used under more alkaline conditions than that of Example 2.
EXAMPLE 4
80 ml of 50% sodium silicate was stirred while 1.6 ml cone, sulphuric acid in 100 ml water was added. To the stirred mixture, 40 ml of ovalbumin was added and stirring continued for 5 minutes. Gelation took several hours after which the gel was aged for a further 48 hours before being broken, washed and dried to produce an albumin/silica gel composite which actively adsorbed proteins.
EXAMPLE 5
1.952 1 of formic acid was added to 20.870 1 of water. A second solution comprising 10.1 1 of sodium silicate and 8.696 1 of water was added to the first over a period of minutes with vigorous stirring. To this was added a solution containing 417.5 g chitosan in 11.305 1 of water and 417.5 ml formic acid and vigorous stirring continued for 8 minutes. The mass gelled within 30 minutes and was aged for 48 hours after which it was broken through a 5 mm sieve into a 3% solution of ammonium hydroxide. The broken gel was allowed to stand in this solution for 24 hours before being washed and dried. After drying the material had a particle size of approximately 2 mm.
EXAMPLE 6
A column 2.5 cm in diameter and 56' cm long was packed with the material of Example 5 and a solution containing 10 milligram/litre of lead was was passed through the material at 15°C. The effluent from the column was analysed and found to contain less than 1 microgram/litre of lead. Similar results were obtained for aluminium.
EXAMPLE 7
A sample of the material prepared in Example 5 was placed in a 1% solution of copper nitrate at 15°C. The solution was analysed before and after equilibrium adsorption. The adsorption capacity for copper was 160 g Cu per g chitosan. Using an acidified solution of copper sulphate the adsorption capacity was similarly measured at 175 mg Cu per gram chitosan.
EXAMPLE 8
A solution of 5 g sodium carboxymethyl cellulose in 100 ml water was added to a solution containing 100 ml sodium silicate and 84 ml water. This was added with vigorous stirring to 200 ml of 10% formic acid. After gelation the mass was allowed to age for 48 hours and then broken into 1.5 % ammonium hydroxide. After standing in this solution overnight it was washed and dried. EXAMPLE 9
A sample of the material of Example 8 was placed in a 1% solution of copper sulphate and the solution analysed before and after equilibrium adsorption. The adsorption capacity for copper was found to be 187 mg/g polymer.

Claims

1. An adsorbent material comprising an inorganic gel and an organic polymer, wherein the polymer is uniformly and intimately distributed throughout the inorganic gel.
2. A material according to Claim 1 wherein the inorganic gel is of silica, silica alumina or alumina.
3. A material according to Claim 1 wherein the organic polymer is starch, dextran, chitosan, carboxymethyl cellulose, sodium carboxymethyl cellulose, polyvinyl alcohol, agar, agarose, carrageenan, gelatin, sodium alginate or albumin.
4. A material according to Claim 1 wherein the organic polymer comprises between 5 and 50% by weight of the material.
5. A process for preparing a material as claimed in any of the preceding claims which comprises forming an unstable inorganic sol which has dissolved therein an organic polymer, mixing vigorously and allowing or causing the unstable inorganic sol to gel entrapping the polymer therein.
6. A process according to Claim 5 wherein the organic polymer is added to a precursor of the inorganic sol.
7. A process according to Claim 5 wherein the organic polymer is added to the inorganic sol before gelation.
8. A process according to Claim 5 wherein the gel is subsequently allowed to age for between 2 and 48 hours.
9. A process according to Claim 5 wherein, the gel is subsequently treated with ammonium hydroxide.
10. An adsorption process utilising an adsorbent material as hereinbefore described.
PCT/GB1989/000245 1988-03-19 1989-03-10 Composite adsorbents WO1989008500A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB8806605 1988-03-19
GB888806605A GB8806605D0 (en) 1988-03-19 1988-03-19 Composite adsorbents

Publications (1)

Publication Number Publication Date
WO1989008500A1 true WO1989008500A1 (en) 1989-09-21

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WO (1) WO1989008500A1 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1992018237A1 (en) * 1991-04-17 1992-10-29 Pharmacia Lkb Biotechnology Ab Process and means for down stream processing
DE4413354A1 (en) * 1994-04-18 1994-10-27 Thomas Dipl Chem Schlieper Process for preparing a buoyant catalyst support based on silica gel
DE4413405A1 (en) * 1994-04-18 1994-10-27 Daub Joachim Dipl Geooek Process for synthesising polymeric catalyst supports based on silica gel and doping thereof with metal compounds
US6017722A (en) * 1991-04-04 2000-01-25 Board Of Regents, The University Of Texas System Luminous bacteria and methods for the isolation, identification and quantitation of toxicants
WO2000050573A1 (en) * 1999-02-22 2000-08-31 Transgene S.A. Method for obtaining a purified viral preparation
US6673563B1 (en) 1991-04-04 2004-01-06 James E. Becvar Luminous bacteria and methods for the isolation, identification and quantitation of toxicants
US6706188B2 (en) 1993-05-03 2004-03-16 Amersham Biociences Ab Process and means for down stream processing
EP1276514B2 (en) 2000-04-25 2009-07-29 The Procter & Gamble Company Absorbent articles comprising a cationic polysaccharide and silicate

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB157414A (en) * 1921-01-10 1922-04-10 Commandit Ges Fuer Tiefbohrtec Improvements in the driving of the injection-air pumps of internal combustion engines
EP0048110A2 (en) * 1980-09-11 1982-03-24 United Kingdom Atomic Energy Authority Selective retention with composite materials
EP0180934A2 (en) * 1984-11-06 1986-05-14 DECHEMA Deutsche Gesellschaft für Chemisches Apparatewesen, Chemische Technik und Biotechnologie e.V. Use of coarse granules of layered silicates as adsorbents for proteins

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB157414A (en) * 1921-01-10 1922-04-10 Commandit Ges Fuer Tiefbohrtec Improvements in the driving of the injection-air pumps of internal combustion engines
EP0048110A2 (en) * 1980-09-11 1982-03-24 United Kingdom Atomic Energy Authority Selective retention with composite materials
EP0180934A2 (en) * 1984-11-06 1986-05-14 DECHEMA Deutsche Gesellschaft für Chemisches Apparatewesen, Chemische Technik und Biotechnologie e.V. Use of coarse granules of layered silicates as adsorbents for proteins

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6017722A (en) * 1991-04-04 2000-01-25 Board Of Regents, The University Of Texas System Luminous bacteria and methods for the isolation, identification and quantitation of toxicants
US7713690B1 (en) 1991-04-04 2010-05-11 Becvar James E Luminous bacteria and methods for the isolation, identification and quantitation of toxicants
US7256009B2 (en) 1991-04-04 2007-08-14 Becvar James E Luminous bacteria and methods for the isolation, identification and quantitation of toxicants
US6673563B1 (en) 1991-04-04 2004-01-06 James E. Becvar Luminous bacteria and methods for the isolation, identification and quantitation of toxicants
US6340572B1 (en) 1991-04-04 2002-01-22 Board Of Regents, The University Of Texas System Kit for the isolation, identification and quantitation of toxicants
EP0922489A2 (en) * 1991-04-17 1999-06-16 Pharmacia Biotech AB Contact element for fluidised bed
EP0922489A3 (en) * 1991-04-17 1999-07-07 Pharmacia Biotech AB Contact element for fluidised bed
US6325937B1 (en) 1991-04-17 2001-12-04 Amersham Pharmacia Biotech Ab Process and means for down stream processing
WO1992018237A1 (en) * 1991-04-17 1992-10-29 Pharmacia Lkb Biotechnology Ab Process and means for down stream processing
US6398963B1 (en) 1991-04-17 2002-06-04 Amersham Pharmacia Biotech Aktiebolag Process and means for down stream processing
US5522993A (en) * 1991-04-17 1996-06-04 Pharmacia Biotech Ab Process and means for down stream processing
US6706188B2 (en) 1993-05-03 2004-03-16 Amersham Biociences Ab Process and means for down stream processing
DE4413405C2 (en) * 1994-04-18 2000-06-08 Joachim Daub Process for the preparation of polymeric catalyst supports based on silica gel and their doping with metal compounds
DE4413405A1 (en) * 1994-04-18 1994-10-27 Daub Joachim Dipl Geooek Process for synthesising polymeric catalyst supports based on silica gel and doping thereof with metal compounds
DE4413354A1 (en) * 1994-04-18 1994-10-27 Thomas Dipl Chem Schlieper Process for preparing a buoyant catalyst support based on silica gel
WO2000050573A1 (en) * 1999-02-22 2000-08-31 Transgene S.A. Method for obtaining a purified viral preparation
US7264958B1 (en) 1999-02-22 2007-09-04 Transgene, S.A. Method for obtaining a purified viral preparation
EP1276514B2 (en) 2000-04-25 2009-07-29 The Procter & Gamble Company Absorbent articles comprising a cationic polysaccharide and silicate

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