EP 1012386 A1 20000628 - METHOD FOR OPTIMIZING EVAPORATION DRYING OF PAPER, RUNNABILITY, AND PAPER QUALITY AS WELL AS DRYER SECTION THAT MAKES USE OF THE METHOD IN A PAPER MACHINE
Title (en)
METHOD FOR OPTIMIZING EVAPORATION DRYING OF PAPER, RUNNABILITY, AND PAPER QUALITY AS WELL AS DRYER SECTION THAT MAKES USE OF THE METHOD IN A PAPER MACHINE
Title (de)
VERFAHREN ZUR OPTIMIERUNG VON VERDAMPFUNGSTROCKNUNG VON PAPIER, GESCHWINDIGKEIT , UND PAPIERQUALITÄT SOWIE EINE TROCKENPARTIE EINER PAPIERMASCHINE ZUR DURCHFÜHRUNG DES VERFAHRENS
Title (fr)
PROCEDE PERMETTANT D'OPTIMISER LE SECHAGE PAR EVAPORATION DU PAPIER, SON APTITUDE AU PASSAGE SUR MACHINE ET SA QUALITE, ET SECTION DE SECHAGE D'UNE MACHINE A PAPIER UTILISANT CE PROCEDE
Publication
Application
Priority
- FI 9800351 W 19980421
- FI 971714 A 19970422
Abstract (en)
[origin: WO9848107A1] A method and an equipment for evaporation drying of the paper web that comes from the press section (10) of a paper machine. The method consists of three successive stages I, II and III that are carried out in the direction of progress of the web (W) as follows: (I) in the first stage, the paper web coming from the press section (10) of the paper machine is heated in a short section (L1) of the paper machine in the machine direction quickly to a temperature of 55...85 DEG C, and web breaks of the relatively moist and, thus, weak web (W) are minimized; (II) after the first stage (I), the main evaporation drying of the web (W) is carried out so that the evaporation efficiency (PE) and the rate of increase in the dry solids content (KA) of the web (W) are substantially higher than in the first stage or in the final stage (III), and the web temperature (TW) does substantially not rise while the drying proceeds (Fig. 4); (III) in the final stage, the drying is continued with a decreasing evaporation efficiency (Fig. 3) and with such an average rate of increase in the dry solids content (KA) of the web (W) in the machine direction as is lower than in the preceding stage (II) but higher than in a conventional cylinder drying with single-wire draw so that the paper quality can be controlled at the same time.
IPC 1-7
IPC 8 full level
D21F 5/04 (2006.01); D21F 5/06 (2006.01); D21F 7/00 (2006.01)
CPC (source: EP)
D21F 5/04 (2013.01)
Designated contracting state (EPC)
AT DE FR GB IT SE
DOCDB simple family (publication)
WO 9848107 A1 19981029; AT E315123 T1 20060215; AU 7045998 A 19981113; CA 2287355 A1 19981029; CA 2287355 C 20070313; DE 69833107 D1 20060330; DE 69833107 T2 20060817; EP 1012386 A1 20000628; EP 1012386 B1 20060104; FI 971714 A0 19970422; FI 971714 A 19981023; JP 2001504175 A 20010327; JP 3604704 B2 20041222
DOCDB simple family (application)
FI 9800351 W 19980421; AT 98917149 T 19980421; AU 7045998 A 19980421; CA 2287355 A 19980421; DE 69833107 T 19980421; EP 98917149 A 19980421; FI 971714 A 19970422; JP 54509598 A 19980421