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US5144093A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for purifying and end-capping polyols made using double metal cyanide catalysts

Assignee: Arch Chemicals Inc
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Filing: 1991-04-29
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Granted: 1992-09-01
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Expires: 2011-04-29
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Abstract

Abstract A process for producing an ethylene oxide-capped polyol which is essentially free of catalyst residues, wherein the polyol is produced using a double metal cyanide catalyst, which comprises after polyol formation the steps of: (a) contacting a catalyst residue(s)- containing polyol with an effective amount of an oxidant (preferably selected from the group consisting of: oxygen-containing gas(es), peroxide(s), acids, and combinations thereof) to cause said catalyst residue(s) to form insoluble residues that are insoluble in the polyol; (b) separating the insoluble residues from the polyol to provide an essentially double metal cyanide catalyst residue-free polyol; (c) treating said double metal cyanide catalyst residue-free polyol with a base to provided a base-treated polyol; (d) contacting said base-treated polyol with ethylene oxide to produce an ethylene oxide-capped polyol containing base, wherein at least a portion of the secondary hydroxyl groups on said polyol are converted into primary hydroxyl groups, and (e) separating said base from said ethylene oxide capped polyol to provide a purified ethylene oxide capped polyol. In another aspect of the invention, the catalyst residue separation step is effected after EO-capping of the polyol.

Inventors

  • 👤 John W. Reisch
  • 👤 Michael M. Martinez
  • 👤 Maurice Raes

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 00:08
CPC Classifications
C; C08; C08G; C08G65/00; C08G65/02; C08G65/26; C08G65/2642; C08G65/2645; C08G65/2663; C08G65/30

Claims Analysis

Total Claims: 20
Claim 1
Independent Claim 209 words
In a process for producing an ethylene oxide-capped polyol which is essentially free of catalyst residues, wherein the polyol is produced using a double metal cyanide catalyst, the improvement which comprises after polyol formation the steps of: (a) contacting a catalyst residue(s)-containing polyol with an effective amount of an oxidant selected from the group consisting of: oxygen-containing gas(es), peroxide(s), sulfuric acid, and combinations thereof, to cause said catalyst residue(s) to form insoluble residues that are insoluble in the polyol, (b) separating the insoluble residues from the polyol by a method selected from the group consisting of filtration and ion exchange separation to provide an essentially double metal cyanide catalyst residue-free polyol, (c) treating said double metal cyanide catalyst residue-free polyol with a base to provide a base-treated polyol, and vacuum stripping said base-treated polyol, (d) contacting said base-treated polyol with ehtylene oxide to produce an ethylene oxide-capped polyol containing base, wherein at least a portion of the secondary hydroxyl groups on said polyol are converted into primary hydroxyl groups, and (e) separating said base from said ethylene oxide capped polyol by a method selected from the group consisting of filtration in the presence of magnesium silicate, extraction, centrafugation, and combinations thereof, to provide a purified ethylene oxide capped polyol.
Claim 2
Dependent Claim 209 words
In a process for producing an ethylene oxide-capped polyol which is essentially free of catalyst residues, wherein the polyol is produced using a double metal cyanide catalyst, the improvement which comprises after polyol formation the steps of: (a) contacting a catalyst residue(s)-containing polyol with an effective amount of an oxidant selected from the group consisting of: oxygen-containing gas(es), peroxide(s), sulfuric acid, and combinations thereof, to cause said catalyst residue(s) to form insoluble residues that are insoluble in the polyol, (b) separating the insoluble residues from the polyol by a method selected from the group consisting of filtration and ion exchange separation to provide an essentially double metal cyanide catalyst residue-free polyol, (c) treating said double metal cyanide catalyst residue-free polyol with a base to provide a base-treated polyol, and vacuum stripping said base-treated polyol, (d) contacting said base-treated polyol with ehtylene oxide to produce an ethylene oxide-capped polyol containing base, wherein at least a portion of the secondary hydroxyl groups on said polyol are converted into primary hydroxyl groups, and (e) separating said base from said ethylene oxide capped polyol by a method selected from the group consisting of filtration in the presence of magnesium silicate, extraction, centrafugation, and combinations thereof, to provide a purified ethylene oxide capped polyol.
Claim 3
Dependent Claim 34 words
The process of claim 1 wherein said base is employed in an amount sufficient to provide a molar ratio of hydroxyl groups on the polyol to equivalents to base of between 1:1 and 500:1.
Claim 4
Dependent Claim 30 words
The process of claim 1 wherein said base is an alkali metal alkoxide or alkaline earth metal alkoxide contains between one and 23 carbon atoms per molecule on said alkoxide.
Claim 5
Dependent Claim 57 words
The process of claim 1 wherein said base is selected from the group consisting of alkalii metal hydroxides, alakaline earth metal hydroxides, alkali metal hydrides, alkaline earth metal hydrides, alkali metal alkoxides containing between one and eight carbon atoms per molecule, alkaline earth metal alkoxides containing between one and eight carbon atoms per molecule, and combinations thereof.
Claim 6
Dependent Claim 36 words
The process of claim 1 wherein said base contains a metal ion selected from the group consisting of the sodium, potassium, lithium, calcium, and magnesium salts of methoxide, ethoxide, propoxide, butoxide, pentoxide, hexaoxide, and combinations thereof.
Claim 7
Dependent Claim 20 words
The process of claim 1 wherein the separation of step (b) is effected using filtration employing an ion exchange resin.
Claim 8
Dependent Claim 33 words
The process of claim 1 wherein a minor amount of magnesium silicate, aluminum silicate, or mixtures thereof, is incorporated into said catalyst residue-containing Polyol in order to facilitate the separation of step (e).
Claim 9
Dependent Claim 26 words
The process of claim 1 which further comprises the additional step of removing any by-product alcohol from said purified polyol by fractionally distilling said purified polyol.
Claim 10
Dependent Claim 22 words
The process of claim 1 wherein said oxidant is selected from the group consisting of hydrogen peroxide, sulfuric acid, and combinations thereof.
Claim 11
Dependent Claim 175 words
In a process for producing an ethylene oxide-capped polyol which is essentially free of catalyst residues, wherein the polyol is produced using a double metal cyanide catalyst, the improvement which comprises after polyol formation the steps of: (a) contacting a catalyst residue(s)-containing polyol with an effective amount of an oxidant selected from the group consisting of: oxygen-containing gas(es), peroxide(s), sulfuric acid, and combinations thereof, to cause said catalyst residue(s) to form insoluble residues that are insoluble in the polyol, (b) treating said insoluble residue-containing polyol with a base to provide a base-treated polyol, and vacuum stripping said base-treated polyol, (c) contacting said base-treated polyol with ethylene oxide to produce an ethylene oxide-capped polyol wherein at least a portion of the secondary hydroxyl groups on said polyol are converted into primary hydroxyl groups, and (d) separating said insoluble residues from said ethylene oxide-capped polyol by a method selected from the group consisting of filtration in the presence of magnesium silicate, extraction, centrafugation, and combinations thereof, to provide a purified polyol which is essentially free of catalyst-residues.
Claim 12
Dependent Claim 175 words
In a process for producing an ethylene oxide-capped polyol which is essentially free of catalyst residues, wherein the polyol is produced using a double metal cyanide catalyst, the improvement which comprises after polyol formation the steps of: (a) contacting a catalyst residue(s)-containing polyol with an effective amount of an oxidant selected from the group consisting of: oxygen-containing gas(es), peroxide(s), sulfuric acid, and combinations thereof, to cause said catalyst residue(s) to form insoluble residues that are insoluble in the polyol, (b) treating said insoluble residue-containing polyol with a base to provide a base-treated polyol, and vacuum stripping said base-treated polyol, (c) contacting said base-treated polyol with ethylene oxide to produce an ethylene oxide-capped polyol wherein at least a portion of the secondary hydroxyl groups on said polyol are converted into primary hydroxyl groups, and (d) separating said insoluble residues from said ethylene oxide-capped polyol by a method selected from the group consisting of filtration in the presence of magnesium silicate, extraction, centrafugation, and combinations thereof, to provide a purified polyol which is essentially free of catalyst-residues.
Claim 13
Dependent Claim 34 words
The process of claim 10 wherein said base is employed in an amount sufficient to provide a molar ratio of hydroxyl groups on the polyol to equivalents of base of between 1:1 and 500:1.
Claim 14
Dependent Claim 30 words
The process of claim 10 wherein said base is an alkali metal alkoxide or alkaline earth metal alkoxide contains between one and 23 carbon atoms per molecule on said alkoxide.
Claim 15
Dependent Claim 57 words
The process of claim 10 wherein said base is selected from the group consisting of alkalii metal hydroxides, alakaline earth metal hydroxides, alkali metal hydrides, alkaline earth metal hydrides, alkali metal alkoxides containing between one and eight carbon atoms per molecule, alkaline earth metal alkoxides containing between one and eight carbon atoms per molecule, and combinations thereof.
Claim 16
Dependent Claim 36 words
The process of claim 10 wherein said base contains a metal ion selected from the group consisting of the sodium, potassium, lithium, calcium, and magnesium salts of methoxide, ethoxide, propoxide, butoxide, pentoxide, hexaoxide, and combinations thereof.
Claim 17
Dependent Claim 20 words
The process of claim 10 wherein the separation of step (d) is effected using filtration employing an ion exchange resin.
Claim 18
Dependent Claim 33 words
The process of claim 10 wherein a minor amount of magnesium silicate, aluminum silicate, or mixtures thereof, is incorporated into said catalyst residue-containing polyol in order to facilitate the separation of step (d).
Claim 19
Dependent Claim 26 words
The process of claim 10 which further comprises the additional step of removing any by-product alcohol from said purified polyol by fractionally distilling said purified polyol.
Claim 20
Dependent Claim 22 words
The process of claim 10 wherein said oxidant is selected from the group consisting of hydrogen peroxide, sulfuric acid, and combinations thereof.

References Cited (Backward Citations)

US3829505A Cited
US3941849A Cited
US4335188A Cited
US4355188A Cited
US4472560A Cited
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US4721818A Cited
US4877906A Cited
EP0406440A1 Cited
JPH02265923A Cited
JPH02265922A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1995-09-01 1996-03-02 1996-09-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1999-09-01 2000-03-02 2000-09-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2003-09-01 2004-03-02 2004-09-01 $7700.00 Window Closed / Lapsed

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