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Process for continuously producing diisopropyl ether

Assignee: Eneos Corp
•
Filing: 1977-12-29
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Granted: 1980-01-08
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Expires: 1997-12-29
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Abstract

Abstract There is disclosed a process for continuously producing diisopropyl ether of high purity from isopropyl alcohol and propylene at a high yield, which comprises the steps of: continuously passing isopropyl alcohol and propylene at a given molar ratio through a first fixed bed filled with particles of strongly acidic cation-exchange resin at a temperature in the range from 100° C. to 130° C.; then passing the reaction mixture through a second fixed bed filled with a water-insoluble, solid, particulate acid-neutralizing agent; and flash-removing unreacted propylene from the mixture, followed by solvent refining and distillation, whereby diisopropyl ether of high purity is continuously obtained at a high yield.

Inventors

  • 👤 Masao Imaizumi

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 18:37
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C41/05; C07C41/06; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/582

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 420 words
In a process for continuously producing diisopropyl ether of high purity from isopropyl alcohol and propylene at a high yield, the improvements comprising the steps of: passing continuously isopropyl alcohol and propylene at a molar ratio of 1:0.5 to 1:3, of isopropyl alcohol to propylene, through a first fixed bed filled with particles of strongly acidic cation-exchange resin having a mean grain diameter of 0.5 to 10 mm at a liquid space velocity of 0.2 to 2 (1/hr) at a temperature from over 100° C. to 130° C. at a pressure ranging from 20 to 50 atmospheres to react with each other; dividing the resultant reaction mixture emerging from said first fixed bed into first and second streams; passing said first stream through a second fixed bed filled with a water-insoluble, solid, particulate, acid-neutralizing agent having a mean grain diameter of 0.1 to 10 mm, at a temperature ranging from 20° to 130° C., said acid-neutralizing agent being selected from the group consisting of MgO, MgO.mH 2 O (m=0 to 0.5), Al 2 O 3 , hydrotalcite (6MgO.Al 2 O 3 .CO 2 .12H 2 O), Al 2 O 3 .mSiO 2 .nH 2 O (m=0.5 to 3, n=1 to 6), Al 2 O 3 .nH 2 O (n=1 to 6), 2.5MgO.Al 2 O 3 .nH 2 O (n=1 to 6), Na 2 O.Al 2 O 3 .nH 2 O (n=1 to 6), and 2MgO.6SiO 2 .nH 2 O (n=1 to 6); recycling said second stream to said first fixed bed filled with said cation-exchange resin; introducing the resultant neutralized mixture from said second fixed bed into a flashing tower and flashing the mixture to remove unreacted propylene from said mixture; distilling the flashed mixture in a multi-stage distillation tower to recover unreacted isopropyl alcohol from the bottom of said distillation tower and obtain an azeotropic mixture comprising isopropyl alcohol and diisopropyl ether from an upper portion of said distillation tower; bringing said azeotropic mixture comprising isopropyl alcohol and diisopropyl ether into contact with a solvent selected from the group consisting of hydrocarbons, water and lower alcohols having from 1 to 4 carbon atoms, thereby separating said azeotropic mixture into a layer of isopropyl alcohol and a layer of diisopropyl ether, said layer of isopropyl alcohol containing said solvent when said solvent is water or the lower alcohol, and said layer of diisopropyl ether containing said solvent when said solvent is hydrocarbons; separating said layers; and distilling said layer of diisopropyl ether, whereby diisopropyl ether of high purity is obtained.
Claim 2
Dependent Claim 420 words
In a process for continuously producing diisopropyl ether of high purity from isopropyl alcohol and propylene at a high yield, the improvements comprising the steps of: passing continuously isopropyl alcohol and propylene at a molar ratio of 1:0.5 to 1:3, of isopropyl alcohol to propylene, through a first fixed bed filled with particles of strongly acidic cation-exchange resin having a mean grain diameter of 0.5 to 10 mm at a liquid space velocity of 0.2 to 2 (1/hr) at a temperature from over 100° C. to 130° C. at a pressure ranging from 20 to 50 atmospheres to react with each other; dividing the resultant reaction mixture emerging from said first fixed bed into first and second streams; passing said first stream through a second fixed bed filled with a water-insoluble, solid, particulate, acid-neutralizing agent having a mean grain diameter of 0.1 to 10 mm, at a temperature ranging from 20° to 130° C., said acid-neutralizing agent being selected from the group consisting of MgO, MgO.mH 2 O (m=0 to 0.5), Al 2 O 3 , hydrotalcite (6MgO.Al 2 O 3 .CO 2 .12H 2 O), Al 2 O 3 .mSiO 2 .nH 2 O (m=0.5 to 3, n=1 to 6), Al 2 O 3 .nH 2 O (n=1 to 6), 2.5MgO.Al 2 O 3 .nH 2 O (n=1 to 6), Na 2 O.Al 2 O 3 .nH 2 O (n=1 to 6), and 2MgO.6SiO 2 .nH 2 O (n=1 to 6); recycling said second stream to said first fixed bed filled with said cation-exchange resin; introducing the resultant neutralized mixture from said second fixed bed into a flashing tower and flashing the mixture to remove unreacted propylene from said mixture; distilling the flashed mixture in a multi-stage distillation tower to recover unreacted isopropyl alcohol from the bottom of said distillation tower and obtain an azeotropic mixture comprising isopropyl alcohol and diisopropyl ether from an upper portion of said distillation tower; bringing said azeotropic mixture comprising isopropyl alcohol and diisopropyl ether into contact with a solvent selected from the group consisting of hydrocarbons, water and lower alcohols having from 1 to 4 carbon atoms, thereby separating said azeotropic mixture into a layer of isopropyl alcohol and a layer of diisopropyl ether, said layer of isopropyl alcohol containing said solvent when said solvent is water or the lower alcohol, and said layer of diisopropyl ether containing said solvent when said solvent is hydrocarbons; separating said layers; and distilling said layer of diisopropyl ether, whereby diisopropyl ether of high purity is obtained.
Claim 3
Dependent Claim 42 words
The improvement in the process as defined in claim 1, wherein a stream consisting essentially of propylene is recovered from the top of said flashing tower and any subsequent flashing towers and is recycled to said first fixed bed of cation-exchange resin.
Claim 4
Dependent Claim 36 words
The improvement in the process as defined in claim 1 wherein a stream consisting essentially of isopropyl alcohol is recovered from said multi-stage distillation tower and is recycled to said first fixed bed of cation-exchange resin.
Claim 5
Dependent Claim 42 words
The improvement in the process as defined in claim 1, wherein a ratio in quantity of fresh isopropyl alcohol and propylene to be fed to said first bed to said second stream to be recycled is from 1:3 to 1:10 by weight.

References Cited (Backward Citations)

US2067385A Cited
US2391084A Cited
US2994720A Cited
US2922822A Cited
GB957000A Cited
DE2403196A1 Cited
NL7704558A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-01-07 1983-07-09 1984-01-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-01-07 1987-07-09 1988-01-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-01-07 1991-07-09 1992-01-08 $7700.00 Window Closed / Lapsed

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