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

Method for controlling drying of a web-formed material

Patent 6938359 Issued on September 6, 2005. Estimated Expiration Date: Icon_subject January 16, 2022. 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

3161482

Method and apparatus for drying wet particulate material to a predetermined uniform moisture content
Patent #: 4696115
Issued on: 09/29/1987
Inventor: Spadafora

Arrangement in material drying systems
Patent #: 4719708
Issued on: 01/19/1988
Inventor: Karlsson ,   et al.

Method and apparatus for drying coated webs Patent #: 5136790
Issued on: 08/11/1992
Inventor: Hagen, et al.

Inventors

Assignee

Application

No. 10467074 filed on 01/16/2002

US Classes:

34/445, With drying parameter control34/446, Temperature or moisture control of material treated or treating gas or vapor34/487, Gas or vapor flow directing or control34/491, Temperature or moisture content of treated material or chamber controls or directs gas or vapor34/492, Gas or vapor flow varied during treatment34/570, With flow control valve34/524With automatic control

Examiners

Primary: Lu, Jiping

Attorney, Agent or Firm

Foreign Patent References

  • 514397 SE 02/01/2001

International Class

F26B003/00

Abstract

A web-formed material (1), preferably a pulp web (1), is passed through a drying plant, comprising blow boxes arranged in a plurality of drying decks, floating above lower blow boxes, which at their upper sides blow out hot process air against the web-formed material (1). Water, in the form of steam, escaping from the web-formed material (1) is discharged by the process air, at least part of which is recirculated (43) whereas the non-recirculated process air is discharged as exhaust air (41) and is replaced by a corresponding portion of supply air (42) with a low water content. The temperature of the process air is controlled (4). If a deviation from the desired dry content of the dried web-formed material (1) is detected (6), the volume flow of the process air (40) is changed by increasing the volume flow of the process air (40) at too low a dry content in the web-formed material (1), and by decreasing the volume flow of the process air (40) at too high a dry content in the web-formed material, for the purpose of rapidly regaining the desired dry content of the dried web-formed material (1).

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