U.S. patents available from 1976 to present.
U.S. patent applications available from 2005 to present.

Recovery of isopropyl acetate and ethanol from an isopropyl acetate, ethanol and water-containing stream

Patent 5059288 Issued on October 22, 1991. Estimated Expiration Date: Icon_subject November 21, 2009. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

1536545

1898737

3578689

Separation of ethyl acetate from ethanol and water by extractive distillation
Patent #: 4379028
Issued on: 04/05/1983
Inventor: Berg ,   et al.

Separation of methanol from acetone by extractive distillation
Patent #: 4501645
Issued on: 02/26/1985
Inventor: Berg ,   et al.

Separation of n-butyl acetate from n-butanol by extractive distillation
Patent #: 4525245
Issued on: 06/25/1985
Inventor: Berg ,   et al.

Separation of isopropyl acetate from isopropanol by extractive distillation
Patent #: 4693789
Issued on: 09/15/1987
Inventor: Berg ,   et al.

Separation of isopropyl acetate from isopropanol by extractive distillation
Patent #: 4698137
Issued on: 10/06/1987
Inventor: Berg

Method to separate polar organic compounds, in particular aliphatic alcohols, from fermentation fluids Patent #: 4715932
Issued on: 12/29/1987
Inventor: Misselhorn ,   et al.

Inventor

Assignee

Application

No. 439830 filed on 11/21/1989

US Classes:

203/43, Utilizing liquid-liquid extracting of distillation product203/73, One a distillation under positive pressure or vacuum203/98, AND RETURNING PRODUCT OF DISTILLATION STEP TO DISTILLATION ZONE560/248, Purification or recovery568/918By plural liquid phase separation

Examiners

Primary: Bascomb, Wilbur L. Jr.

Attorney, Agent or Firm

Foreign Patent References

  • 125575 EP 11/13/1984
  • 54-119411 JP. 09/13/1979

International Classes

B01D 003/16
C07C 029/86
C07C 067/58

Abstract

High purity isopropyl acetate and ethanol are recovered from a process stream containing isopropyl acetate, ethanol and water by a multiple step process including extracting substantially all of the ethanol from the stream using water as a solvent, stripping the extract stream to remove substantially all of the remaining isopropyl acetate as an overhead recycle stream, which is combined with the fresh feed stream prior to the extraction step, fractionating the ethanol-rich stripping column bottoms stream to produce a ethanol-water azeotropic overhead stream and using a portion of the fractionating column bottoms stream as the solvent for the extraction step.

Other References

  • 79.09.17, J54119411, JP 54-11941
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