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

Emulsifying and separating latex and solvent

Patent 4115316 Issued on September 19, 1978. Estimated Expiration Date: Icon_subject June 28, 1996. 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

2350609

3268501

3583967

Inventor

Assignee

Application

No. 05/700295 filed on 06/28/1976

US Classes:

366/69, RUBBER OR HEAVY PLASTIC WORKING159/16.3, Steam injection528/500, Steam stripping or steam distilling528/501With distilling or pressured reduction step to remove material, e.g., flashing, autorefrigeration, etc.

Examiners

Primary: Yudkoff, Norman

Attorney, Agent or Firm

International Classes

C08J 3/03 (20060101)
C08J 3/02 (20060101)
B01F 17/00 (20060101)
B01D 3/34 (20060101)

Abstract

This process relates to the preparation of stable aqueous latices from solvent dispersions of elastomers and other high polymer compositions. The process in common with that of earlier applications is characterized, inter alia, by the establishment of a flow of gas comprising steam as a continuous phase into which an emulsion of a cement of the polymer is dispersed as an aerosol of latex droplets in a solvent-vapor continuum, followed by coalescence of the latex droplets and separation of the resulting coalesced liquid phase from the resulting solvent-vapor phase.In the present disclosure, special provisions are made for generating from recovered water saturated with solvent (and possibly contaminated with carry-over of macromolecular material and/or emulsifier and/or latex droplets) the gas comprising steam employed in forming the initial continous phase. By this process it is possible to essentially exclude or eliminate the continuous supply of external steam to the process and the disposal of the condensate resulting therefrom. In the preferred practice of these provisions the quantity of water supplied to the process thus can be reduced essentially to only that quantity of water constituting the aqueous phase of the latex product withdrawn from the process, and environmental polution with process effluent liquid and solid materials may be avoided or greatly minimized.Furthermore, in preferred embodiments the process utilizes material carried over in or with the vapors and inhibits process solid and solvent losses and thus increases the efficiency of the process.

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