Restrained paper dryer

• US 5,588,223 A
• Filed: 06/14/1994
• Issued: 12/31/1996
• Est. Priority Date: 06/14/1994
• Status: Expired due to Fees

• Current Assignee: Asea Brown Boveri AB (ABB Limited)
• Original Assignee: Asea Brown Boveri AB (ABB Limited)
• Inventors: Marshall, Hugh G.
• Primary Examiner(s): Bennett, Henry A.
• Assistant Examiner(s): GRAVINI, STEPHEN MICHAEL
• Application Number:
  US08/259,503
• Time in Patent Office: 931 Days
• Field of Search: 34/306, 34/361, 34/362, 34/363, 34/414, 34/430, 34/444, 34/481, 34/487, 34/111, 34/112, 34/122, 34/123, 34/135, 34/629, 34/635, 34/636
• US Class Current: 34/414
• CPC Class Codes: D21F 5/181 on Yankee cylinder
• CPC Class Codes: D21F 5/185 Supporting webs in hot air dryers
• CPC Class Codes: F26B 13/101 Supporting materials without tension, e.g. on or between foraminous belts
• CPC Class Codes: F26B 13/18 heated or cooled, e.g. from inside, the material being dried on the outside surface by conduction

Abstract

Methods and apparatus are disclosed for restrained paper drying in order to produce high performance paper with enhanced stiffness and, in the process, substantially improve paper properties and reduce fiber usage. The paper web is held in a restrained position on a fabric by air suction imposed from beneath the web and is of sufficient application to prevent shrinkage of the web. The web is simultaneously dried by high velocity, high temperature air or superheated steam. For improved finish properties, the wet paper web may be pressed onto a polished heated metal cylinder with restraint being imposed by gluing.

Claims

1. An improved method of drying a moving paper web in an elongated drying apparatus comprising the steps of:

a) holding the web in a restrained position on an open weave fabric by means of air suction from 3 to 12 inches H₂ O imposed progressively along the length of the drying apparatus from underneath the web and sufficient to prevent shrinkage of the web; and

b) applying a drying medium to said web in the form of high temperature, high velocity air or superheated steam, whereby shrinkage of said web is substantially inhibited, ring crush strength is increased and fibre requirements are reduced.

2. A method according to claim 1 wherein the high velocity, high temperature air or superheated steam is applied to the web at approximately 25,000 fpm and 600°

to 800°

F.

3. A method according to claim 1 wherein the paper web enters the restrained drying apparatus at approximately 55% dry and is removed from the restrained drying apparatus at 75% or 93% dry.

4. Apparatus for drying and moving paper web comprising:

an elongated module having a plurality of drying nozzles spaced throughout the length of said module;

a suction box arranged opposite said module and the drying nozzles therein and defining a path of travel for said paper web between said nozzles and the suction box;

means in said suction box for providing support for a fabric, web-supporting belt;

means for delivering high velocity, high temperature air or superheated steam to said nozzles for impingement against at least one surface of said web; and

means for simultaneously applying suction from 3 to 12 inches H₂ O, progressively throughout the length of said suction box, to the other surface of said web sufficient to prevent shrinkage thereof during drying.

5. Apparatus according to claim 4 wherein said module includes present headers to distribute said drying medium to said nozzle;

means for providing a source for said drying medium; and

duct means for transmitting said medium to said module and the headers therein;

said nozzles being segmented to control the drying process.

6. Apparatus according to claim 5 wherein said drying medium is high velocity, high temperature air or superheated steam applied by said nozzles against the web at approximately 25,000 fpm and 600°

to 800°

F.

7. Apparatus according to claim 4 wherein said fabric support means in said suction box comprises a plurality of rollers spaced along the length of said suction box.

8. Apparatus according to claim 4 wherein said fabric support means in the suction box comprises a plurality of fabric blades with water spaced throughout the length of said suction box.

9. An improved method of drying a moving paper web in an elongated multi-pass drying apparatus comprising the steps of:

a) holding the web in a restrained position on an open weave fabric by means of air suction from 3 to 12 inches H₂ O imposed progressively along the length of each pass of the multi-pass drying apparatus from underneath the web and sufficient to prevent shrinkage of the web; and

b) applying a drying medium to said web along each pass of the multi-pass apparatus in the form of high temperature, high velocity air or superheated steam, whereby shrinkage of said web is substantially inhibited, ring crush strength is increased and fibre requirements are reduced.

10. A method according to claim 9 wherein the high velocity, high temperature air or superheated steam is applied to the web at approximately 25,000 fpm and 600°

to 800°

F.

11. A method according to claim 9 wherein the paper web enters the multi-pass restrained drying apparatus at approximately 55% dry and is removed from the restrained drying apparatus at 75% or 93% dry.

12. Apparatus for drying a moving paper web comprising:

a housing enclosing a plurality of jet impingement blow boxes arranged in a stack and each having a plurality of drying nozzles spaced throughout the length of the box;

a plurality of suction boxes arranged in the stack intermediate said jet impingement blow boxes;

said blow boxes and suction boxes defining between them a path of travel for said paper web;

means in said suction boxes for providing support for a fabric, web-supporting belt;

suction turning and guide rolls at each end of said suction boxes for turning and guiding said fabric and web;

means for delivering high velocity, high temperature air or superheated steam to said nozzles for impingement against at least one surface of said web on each pass of the apparatus; and

means for simultaneously applying suction from 3 to 12 inches H₂ O, progressively throughout the length of said suction boxes, to the other surface of said web sufficient to prevent shrinkage thereof during drying.

13. Apparatus according to claim 12 wherein said drying medium is high velocity, high temperature air or superheated steam applied by said nozzles against the web at approximately 25,000 fpm and 600°

to 800°

F.

14. Apparatus according to claim 12 wherein said jet impingement blow boxes are hingedly mounted in said housing so as to provide servicing access to the paths of travel of said web.