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US5166123A Expired / Lapsed US ⏱️ 0.0 years remaining

Carbonaceous adsorbent for removal of pyrogen from water

Assignee: Tokyo Organic Chemical Industries Inc
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Filing: 1990-12-05
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Granted: 1992-11-24
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Expires: 2010-12-05
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Abstract

Abstract A carbonaceous adsorbent to be used for the removal of a pyrogen dissolved in water is disclosed. The adsorbent is obtained by carbonizing porous beads of a cross-linked polymer. This adsorbent is favorably used for the removal of endotoxin in the production of pure water from deionized water resulting from the treatment with ion-exchange resins.

Inventors

  • 👤 Wataru Agui
  • 👤 Shuji Tamura
  • 👤 Hiroshi Kuyama
  • 👤 Yoshiya Kurachi
  • 👤 Masahiko Abe
  • 👤 Yukihiro Kaneko
  • 👤 Keizo Ogino

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 19:57
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/28; C02F1/283; B; B01; B01J; B01J20/00; B01J20/02; B01J20/20; C02F2103/00; C02F2103/02; C02F2103/04

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 231 words
A carbonaceous adsorbent for the removal of pyrogens dissolved in pure water, which absorbent is produced by suspension polymerizing styrene and divinyl benzene in the presence of an additive selected from the group consisting of (i) a precipitant solvent which is incapable of swelling the cross-linked styrene copolymer produced, (ii) solvents which are soluble in styrene and which are capable of swelling the cross-linked styrene copolymer, (iii) mixed solvents simultaneously containing solvents (i) and (ii), (iv) organic liquids formed of said solvent capable of swelling the cross-linked styrene copolymer product and styrene linear polymers capable of forming a homogeneous liquid phase with the swelling agents, and (v) macromolecules which are soluble in styrene-divinyl benzene mixtures and inactive to the cross-linked styrene copolymer produced in an amount sufficient to acquire porosity, thereby producing cross-linked polymer beads of a given skeletal structure; subjecting the resulting porous cross-linked styrene copolymer beads to sulfonation with fuming sulfuric acid; infusibilizing the thus-treated cross-linked styrene copolymer beads with sulfuric acid, nitrogen dioxide or chlorine; carbonizing the infusibilized copolymer beams by calcining the beads at a temperature in a range of 300°-900° C.; and activating the carbonized beads by steam, thereby producing an adsorbent which retains the skeletal structure of the copolymer beads intact and which is capable of reducing the pyrogenic content of water containing the same to at least the pyrogen detection limit of 0.01 ng/ml.
Claim 2
Dependent Claim 231 words
A carbonaceous adsorbent for the removal of pyrogens dissolved in pure water, which absorbent is produced by suspension polymerizing styrene and divinyl benzene in the presence of an additive selected from the group consisting of (i) a precipitant solvent which is incapable of swelling the cross-linked styrene copolymer produced, (ii) solvents which are soluble in styrene and which are capable of swelling the cross-linked styrene copolymer, (iii) mixed solvents simultaneously containing solvents (i) and (ii), (iv) organic liquids formed of said solvent capable of swelling the cross-linked styrene copolymer product and styrene linear polymers capable of forming a homogeneous liquid phase with the swelling agents, and (v) macromolecules which are soluble in styrene-divinyl benzene mixtures and inactive to the cross-linked styrene copolymer produced in an amount sufficient to acquire porosity, thereby producing cross-linked polymer beads of a given skeletal structure; subjecting the resulting porous cross-linked styrene copolymer beads to sulfonation with fuming sulfuric acid; infusibilizing the thus-treated cross-linked styrene copolymer beads with sulfuric acid, nitrogen dioxide or chlorine; carbonizing the infusibilized copolymer beams by calcining the beads at a temperature in a range of 300°-900° C.; and activating the carbonized beads by steam, thereby producing an adsorbent which retains the skeletal structure of the copolymer beads intact and which is capable of reducing the pyrogenic content of water containing the same to at least the pyrogen detection limit of 0.01 ng/ml.
Claim 3
Dependent Claim 17 words
The adsorbent of claim 1, wherein the sulfonation and infusibilization are simultaneously conducted with fuming sulfuric acid.
Claim 4
Dependent Claim 17 words
The adsorbent of claim 1, wherein the adsorbent has a surface area of 345-1,100 m 3 /g.
Claim 5
Dependent Claim 234 words
A carbonaceous adsorbent for the removal of pyrogens dissolved in pure water, which adsorbent is produced by suspension polymerizing styrene and divinyl benzene in the presence of an additive selected from the group consisting of (i) a precipitant solvent which is incapable of swelling the cross-linked styrene copolymer produced, (ii) solvents which are soluble in styrene and which are capable of swelling the cross-linked styrene copolymer, (iii) mixed solvents simultaneously containing solvents (i) and (ii), (iv) organic liquids formed of said solvent capable of swelling the cross-linked styrene copolymer product and styrene linear polymers capable of forming a homogenous liquid phase with the swelling agents, and (v) macromolecules which are soluble in styrene-divinyl benzene mixtures and inactive to the cross-linked styrene copolymer produced in an amount sufficient to acquire porosity, thereby producing cross-linked polymer beads of a given skeletal structure; subjecting the resulting porous cross-linked styrene copolymer beads to sulfonation with fuming sulfuric acid; infusibilizing the thus-treated cross-linked styrene copolymer beads with sulfuric acid, nitrogen dioxide or chlorine; carbonizing the infusibilized copolymer beads by calcining the beads at a temperature in a range of 300°-900° C.; and activating the carbonized beads with aqueous ZnCl 2 , thereby producing an adsorbent which retains the skeletal structure of the copolymer beads intact and which is capable of reducing the pyrogenic content of water containing the same to at least the pyrogen detection limit of 0.01 ng/ml.
Claim 6
Dependent Claim 234 words
A carbonaceous adsorbent for the removal of pyrogens dissolved in pure water, which adsorbent is produced by suspension polymerizing styrene and divinyl benzene in the presence of an additive selected from the group consisting of (i) a precipitant solvent which is incapable of swelling the cross-linked styrene copolymer produced, (ii) solvents which are soluble in styrene and which are capable of swelling the cross-linked styrene copolymer, (iii) mixed solvents simultaneously containing solvents (i) and (ii), (iv) organic liquids formed of said solvent capable of swelling the cross-linked styrene copolymer product and styrene linear polymers capable of forming a homogenous liquid phase with the swelling agents, and (v) macromolecules which are soluble in styrene-divinyl benzene mixtures and inactive to the cross-linked styrene copolymer produced in an amount sufficient to acquire porosity, thereby producing cross-linked polymer beads of a given skeletal structure; subjecting the resulting porous cross-linked styrene copolymer beads to sulfonation with fuming sulfuric acid; infusibilizing the thus-treated cross-linked styrene copolymer beads with sulfuric acid, nitrogen dioxide or chlorine; carbonizing the infusibilized copolymer beads by calcining the beads at a temperature in a range of 300°-900° C.; and activating the carbonized beads with aqueous ZnCl 2 , thereby producing an adsorbent which retains the skeletal structure of the copolymer beads intact and which is capable of reducing the pyrogenic content of water containing the same to at least the pyrogen detection limit of 0.01 ng/ml.
Claim 7
Dependent Claim 17 words
The adsorbent of claim 4, wherein the sulfonation and infusibilization are simultaneously conducted with fuming sulfuric acid.
Claim 8
Dependent Claim 230 words
A carbonaceous adsorbent for the removal of pyrogens dissolved in pure water, which adsorbent is produced by suspension polymerizing styrene and divinyl benzene in the presence of an additive selected from the group consisting of (i) a precipitant solvent which is incapable of swelling the cross-linked styrene copolymer produced, (ii) solvents which are soluble in styrene and which are capable of swelling the cross-linked styrene copolymer, (iii) mixed solvents simultaneously containing solvents (i) and (ii), (iv) organic liquids formed of said solvent capable of swelling the cross-linked styrene copolymer product and styrene linear polymers capable of forming a homogeneous liquid phase with the swelling agents, and (v) macromolecules which are soluble in styrene-divinyl benzene mixtures and inactive to the cross-linked styrene copolymer produced in an amount sufficient to acquire porosity, thereby producing cross-linked polymer beads of a given skeletal structure; subjecting the resulting porous cross-linked styrene copolymer beads to chloromethylation followed by amination; infusibilizing the thus-treated cross-linked styrene copolymer beads with sulfuric acid, nitrogen dioxide or chlorine; carbonizing the infusibilized copolymer beads by calcining the beads at a temperature in a range of 300°-900° C.; and activating the carbonized beads by steam, thereby producing an adsorbent which retains the skeletal structure of the copolymer beads intact and which is capable of reducing the pyrogenic content of water containing the same to at least the pyrogen detection limit of 0.01 ng/ml.
Claim 9
Dependent Claim 230 words
A carbonaceous adsorbent for the removal of pyrogens dissolved in pure water, which adsorbent is produced by suspension polymerizing styrene and divinyl benzene in the presence of an additive selected from the group consisting of (i) a precipitant solvent which is incapable of swelling the cross-linked styrene copolymer produced, (ii) solvents which are soluble in styrene and which are capable of swelling the cross-linked styrene copolymer, (iii) mixed solvents simultaneously containing solvents (i) and (ii), (iv) organic liquids formed of said solvent capable of swelling the cross-linked styrene copolymer product and styrene linear polymers capable of forming a homogeneous liquid phase with the swelling agents, and (v) macromolecules which are soluble in styrene-divinyl benzene mixtures and inactive to the cross-linked styrene copolymer produced in an amount sufficient to acquire porosity, thereby producing cross-linked polymer beads of a given skeletal structure; subjecting the resulting porous cross-linked styrene copolymer beads to chloromethylation followed by amination; infusibilizing the thus-treated cross-linked styrene copolymer beads with sulfuric acid, nitrogen dioxide or chlorine; carbonizing the infusibilized copolymer beads by calcining the beads at a temperature in a range of 300°-900° C.; and activating the carbonized beads by steam, thereby producing an adsorbent which retains the skeletal structure of the copolymer beads intact and which is capable of reducing the pyrogenic content of water containing the same to at least the pyrogen detection limit of 0.01 ng/ml.
Claim 10
Dependent Claim 17 words
The adsorbent of claim 6, wherein the adsorbent has a surface area of 345-1,100 m 3 /g.
Claim 11
Dependent Claim 233 words
A carbonaceous adsorbent for the removal of pyrogens dissolved in pure water, which adsorbent is produced by suspension polymerizing styrene and divinyl benzene in the presence of an additive selected from the group consisting of (i) a precipitant solvent which is incapable of swelling the cross-linked styrene copolymer produced, (ii) solvents which are soluble in styrene and which are capable of swelling the cross-linked styrene copolymer, (iii) mixed solvents simultaneously containing solvents (i) and (ii), (iv) organic liquids formed of said solvent capable of swelling the cross-linked styrene copolymer product and styrene linear polymers capable of forming a homogeneous liquid phase with the swelling agents, and (v) macromolecules which are soluble in styrene-divinyl benzene mixtures and inactive to the cross-linked styrene copolymer produced in an amount sufficient to acquire porosity, thereby producing cross-linked polymer beads of a given skeletal structure; subjecting the resulting porous cross-linked styrene copolymer beads to chloromethylation followed by amination; infusibilizing the thus-treated cross-linked styrene copolymer beads with sulfuric acid, nitrogen dioxide or chlorine; carbonizing the infusibilized copolymer beads by calcining the beads at a temperature in a range of 300°-900° C.; and activating the carbonized beads with aqueous ZnCl 2 , thereby producing an adsorbent which retains the skeletal structure of the copolymer beads intact and which is capable of reducing the pyrogenic content of water containing the same to at least the pyrogen detection limit of 0.01 ng/ml.
Claim 12
Dependent Claim 233 words
A carbonaceous adsorbent for the removal of pyrogens dissolved in pure water, which adsorbent is produced by suspension polymerizing styrene and divinyl benzene in the presence of an additive selected from the group consisting of (i) a precipitant solvent which is incapable of swelling the cross-linked styrene copolymer produced, (ii) solvents which are soluble in styrene and which are capable of swelling the cross-linked styrene copolymer, (iii) mixed solvents simultaneously containing solvents (i) and (ii), (iv) organic liquids formed of said solvent capable of swelling the cross-linked styrene copolymer product and styrene linear polymers capable of forming a homogeneous liquid phase with the swelling agents, and (v) macromolecules which are soluble in styrene-divinyl benzene mixtures and inactive to the cross-linked styrene copolymer produced in an amount sufficient to acquire porosity, thereby producing cross-linked polymer beads of a given skeletal structure; subjecting the resulting porous cross-linked styrene copolymer beads to chloromethylation followed by amination; infusibilizing the thus-treated cross-linked styrene copolymer beads with sulfuric acid, nitrogen dioxide or chlorine; carbonizing the infusibilized copolymer beads by calcining the beads at a temperature in a range of 300°-900° C.; and activating the carbonized beads with aqueous ZnCl 2 , thereby producing an adsorbent which retains the skeletal structure of the copolymer beads intact and which is capable of reducing the pyrogenic content of water containing the same to at least the pyrogen detection limit of 0.01 ng/ml.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1995-11-24 1996-05-25 1996-11-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1999-11-24 2000-05-25 2000-11-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2003-11-24 2004-05-25 2004-11-24 $7700.00 Window Closed / Lapsed

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