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

Method and apparatus for drying coated webs

Patent 5136790 Issued on August 11, 1992. Estimated Expiration Date: Icon_subject March 7, 2011. 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

Paint drying oven
Patent #: 4164819
Issued on: 08/21/1979
Inventor: Devillard

Process for heat-treating a fabric web
Patent #: 4231165
Issued on: 11/04/1980
Inventor: Gresens ,   et al.

Methods for controlling vapor concentrations in an atmosphere
Patent #: 4337582
Issued on: 07/06/1982
Inventor: Smith

Catalytic solvent vapor incinerating apparatus
Patent #: 4343769
Issued on: 08/10/1982
Inventor: Henkelmann

Process for drying and curing wire insulation using heat exchange and apparatus therefor
Patent #: 4475294
Issued on: 10/09/1984
Inventor: Henricks

Hot air dryer structure
Patent #: 4575952
Issued on: 03/18/1986
Inventor: Bodenan ,   et al.

Process for drying coated web
Patent #: 4894927
Issued on: 01/23/1990
Inventor: Ogawa, et al.

Control system for air flotation dryer with a built-in afterburner Patent #: 4942676
Issued on: 07/24/1990
Inventor: Wimberger, et al.

Inventors

Application

No. 666857 filed on 03/07/1991

US Classes:

34/444, Sheet, web, or strand34/79Separation of substances from treating or exhaust gases or vapors

Examiners

Primary: Bennett, Henry
Assistant: Gromada, Denise L.

Attorney, Agent or Firm

International Class

F26B 003/00

Abstract

A method and apparatus for drying a continuously moving web carrying a liquid, wherein the web is passed through a dryer in which the web is exposed to a recirculating flow of heated drying gas. Exhaust gas is diverted and discharged from the recirculating gas flow at a flow rate which is variable between maximum and minimum levels, and makeup gas is added to the recirculating gas flow at a flow rate which is also variable between maximum and minimum levels. A process variable is sensed and compared to a selected set point. A first of the aforesaid flow rates is adjusted to maintain the process variable at the selected set point, and a second of the aforesaid flow rates is adjusted in response to adjustments to the first flow rate in order to insure that the first flow rate remains between its maximum and minimum levels.

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