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US4798674A Expired / Lapsed US ⏱️ 0.0 years remaining

Separation of organic liquids

Assignee: Texaco Inc
•
Filing: 1988-03-10
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Granted: 1989-01-17
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Expires: 2008-03-10
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Abstract

Abstract Mixtures containing methanol and dimethyl carbonate or methanol and methyl t-butyl ether may be treated by pervaporation to recover product containing decreased quantity of methanol.

Inventors

  • 👤 Mordechai Pasternak
  • 👤 Craig R. Bartels
  • 👤 John Reale, Jr.

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 15:47
CPC Classifications
B; B01; B01D; B01D67/00; B01D67/0081; B01D67/0093; B01D61/00; B01D61/36; B01D61/362; B01D71/00; B01D71/06; B01D71/38; B01D71/381; C; C07; C07C; C07C29/00; C07C29/74; C07C29/76; C07C41/00; C07C41/01; C07C41/34; C07C41/36; C07C45/00; C07C45/78; C07C45/786; C07C68/00; C07C68/08; B01D2323/00; B01D2323/30

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 306 words
The method comprising: concentrating a charge solution containing (i) an alcohol having less than three carbon atoms and (ii) an oxygenate selected from the group consisting of organic ethers, aldehydes, ketones, and esters by, maintaining a non-porous membrane separating layer selected from the group consisting of (i) polyvinyl alcohol which has been crosslinked with an aliphatic polyaldehyde containing at least three carbon atoms including those in said aldehyde groups; and (ii) high molecular weight ion exchange resin in membrane form having carbon atoms in the backbone bearing a pendant acid group, which membrane has been contacted with a quaternary ammonium salt containing four hydrocarbyl groups; maintaining a pressure drop across said non-porous separating layer; passing a charge aqueous solution containing (i) an alcohol having less than three carbon atoms and (ii) an oxygenate selected from the group consisting of organic ethers, aldehydes, ketones, and esters into contact with the high pressure side of said non-porous separating layer having properties which enable at least a portion of said alcohol in said charge solution and a lesser portion of oxygenate to pass by pervaporation through said non-porous separating layer as a lean mixture containing more alcohol and less oxygenate than are present in said charge solution and said charge solution is converted to a rich liquid containing less alcohol and more oxygenate than are present in said charge solution; recovering as permeate from the low pressure side of said non-porous separating layer said lean mixture containing more alcohol and less oxygenate than are present in said charge solution, said lean mixture being recovered in vapor phase at a pressure below the vapor pressure thereof; and recovering as retentate from the high pressure side of said non-porous separating layer said rich liquid containing a lower alcohol content and a high oxygenate content than are present in said charge solution.
Claim 2
Independent Claim 306 words
The method comprising: concentrating a charge solution containing (i) an alcohol having less than three carbon atoms and (ii) an oxygenate selected from the group consisting of organic ethers, aldehydes, ketones, and esters by, maintaining a non-porous membrane separating layer selected from the group consisting of (i) polyvinyl alcohol which has been crosslinked with an aliphatic polyaldehyde containing at least three carbon atoms including those in said aldehyde groups; and (ii) high molecular weight ion exchange resin in membrane form having carbon atoms in the backbone bearing a pendant acid group, which membrane has been contacted with a quaternary ammonium salt containing four hydrocarbyl groups; maintaining a pressure drop across said non-porous separating layer; passing a charge aqueous solution containing (i) an alcohol having less than three carbon atoms and (ii) an oxygenate selected from the group consisting of organic ethers, aldehydes, ketones, and esters into contact with the high pressure side of said non-porous separating layer having properties which enable at least a portion of said alcohol in said charge solution and a lesser portion of oxygenate to pass by pervaporation through said non-porous separating layer as a lean mixture containing more alcohol and less oxygenate than are present in said charge solution and said charge solution is converted to a rich liquid containing less alcohol and more oxygenate than are present in said charge solution; recovering as permeate from the low pressure side of said non-porous separating layer said lean mixture containing more alcohol and less oxygenate than are present in said charge solution, said lean mixture being recovered in vapor phase at a pressure below the vapor pressure thereof; and recovering as retentate from the high pressure side of said non-porous separating layer said rich liquid containing a lower alcohol content and a high oxygenate content than are present in said charge solution.
Claim 3
Dependent Claim 18 words
The method claimed in claim 1 wherein said aliphatic polyaldehyde is a C 1 -C 6 aliphatic dialdehyde.
Claim 4
Dependent Claim 12 words
The method claimed in claim 1 wherein said aliphatic polyaldehyde is glutaraldehyde.
Claim 5
Dependent Claim 11 words
The method claimed in claim 1 wherein said alcohol is methanol.
Claim 6
Dependent Claim 15 words
The method claimed in claim 1 wherein said charge solution contains methanol and dimethyl carbonate.
Claim 7
Dependent Claim 16 words
The method claimed in claim 1 wherein said charge solution contains methanol and methyl t-butyl ether.
Claim 8
Dependent Claim 19 words
The method claimed in claim 1 wherein said separating layer is polyvinyl alcohol which has been crosslinked with glutaraldehyde.
Claim 9
Dependent Claim 49 words
The method claimed in claim 1 wherein said separating layer is a high molecular weight ion exchange resin in membrane form having carbon atoms in the backbone bearing a pendant acid group, which resin is characterized by the formula: ##STR8## said membrane having been contacted with tetramethyl ammonium halide.
Claim 10
Independent Claim 248 words
The method comprising: concentrating a charge solution containing methanol and either dimethyl carbonate or methyl t-butyl ether oxygenate by, maintaining a membrane of non-porous separating layer of cast polyvinyl alcohol which has been crosslinked with an aliphatic polyaldehyde containing at least three carbon atoms including those in said aldehyde groups; maintaining a pressure drop across said non-porous separating layer of polyvinyl alcohol; passing a charge aqueous solution containing methanol and either dimethyl carbonate or methyl t-butyl ether oxygenate into contact with the high pressure side of said non-porous separating layer of polyvinyl alcohol having properties which enable at least a portion of said methanol in said charge solution and a lesser portion of oxygenate to pass by pervaporation through said non-porous separating layer of polyvinyl alcohol as a lean mixture containing more methanol and less oxygenate than are present in said charge solution and said charge solution is converted to a rich liquid containing less methanol and more oxygenate than are present in said charge solution; recovering as permeate from the low pressure side of said non-porous separating layer of polyvinyl alcohol said lean mixture containing more methanol and less oxygenate than are present in said charge solution, said lean mixture being recovered in vapor phase at a pressure below the vapor pressure thereof; and recovering as retentate from the high pressure side of said non-porous separating layer said rich liquid containing a lower methanol content and a higher oxygenate content than are present in said charge solution.
Claim 11
Independent Claim 248 words
The method comprising: concentrating a charge solution containing methanol and either dimethyl carbonate or methyl t-butyl ether oxygenate by, maintaining a membrane of non-porous separating layer of cast polyvinyl alcohol which has been crosslinked with an aliphatic polyaldehyde containing at least three carbon atoms including those in said aldehyde groups; maintaining a pressure drop across said non-porous separating layer of polyvinyl alcohol; passing a charge aqueous solution containing methanol and either dimethyl carbonate or methyl t-butyl ether oxygenate into contact with the high pressure side of said non-porous separating layer of polyvinyl alcohol having properties which enable at least a portion of said methanol in said charge solution and a lesser portion of oxygenate to pass by pervaporation through said non-porous separating layer of polyvinyl alcohol as a lean mixture containing more methanol and less oxygenate than are present in said charge solution and said charge solution is converted to a rich liquid containing less methanol and more oxygenate than are present in said charge solution; recovering as permeate from the low pressure side of said non-porous separating layer of polyvinyl alcohol said lean mixture containing more methanol and less oxygenate than are present in said charge solution, said lean mixture being recovered in vapor phase at a pressure below the vapor pressure thereof; and recovering as retentate from the high pressure side of said non-porous separating layer said rich liquid containing a lower methanol content and a higher oxygenate content than are present in said charge solution.

References Cited (Backward Citations)

US4113780A Cited
US4590098A Cited
US4618534A Cited
US4600751A Cited
US4728429A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1992-01-17 1992-07-18 1993-01-17 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1996-01-17 1996-07-18 1997-01-17 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2000-01-17 2000-07-18 2001-01-17 $7700.00 Window Closed / Lapsed

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