公开(公告)号：FR2465818A1

公开(公告)日：1981-03-27

申请号：FR8020512

申请日：1980-09-24

Applicant: ICI LTD ,  IMPERIAL CHEMICAL IND LTD

Inventor： PORTER KENNETH ,  KENNETH PORTER

IPC: D04H1/52 ,  D04H3/02 ,  D04B23/10 ,  D04H3/10 ,  D04H3/04

Abstract: MACHINE COMPRENANT UN DISPOSITIF D'AMENEE D'UNE COUCHE DE CHAINE 7, UN DISPOSITIF D'ALIMENTATION EN CONTINU D'UN FIL DE TRAME 11, UN DISPOSITIF D'ALIMENTATION EN PLUSIEURS FILS DE COUTURE 10 ET UN DISPOSITIF DE COUTURE DE LA COUCHE DE CHAINE 7 ET DU FIL DE TRAME 11 L'UNE AVEC L'AUTRE A L'AIDE DES FILS CORRESPONDANTS 10. LE DISPOSITIF D'ALIMENTATION ET DE POSE DU FIL DE TRAME 10 CONSISTE EN DEUX PLAQUES 4 ETROITEMENT RAPPROCHEES, EN ELEMENTS DESTINES A FAIRE AVANCER UN FIL INDIVIDUEL 11 VERS LES PLAQUES 4 ET EN ELEMENTS DESTINES A IMPOSER UN MOUVEMENT OSCILLANT AU FIL 11 QUI AVANCE AVANT SON PASSAGE ENTRE LES PLAQUES 4. APPLICATION A LA PRODUCTION D'ETOFFES NON TISSEES COMPRENANT UNE CHAINE ET UNE TRAME LIEES PAR COUTURE.

公开(公告)号：FR2463220A2

公开(公告)日：1981-02-20

申请号：FR8017987

申请日：1980-08-14

Applicant: ICI LTD

Inventor： PORTER KENNETH

IPC: D04H3/05 ,  D04H3/02

Abstract: An apparatus for laying down a fibrous strand (1) in an ordered configuration comprising means (2) for supplying a fibrous strand, means (4) for forwarding the strand, means (7) to impart an oscillatory motion to the forwarding strand and a moveable collecting surface (11) whereon the strand is laid such apparatus including two closely spaced shaped plates (10) which extend between the oscillating means (7) and the collecting surface (11).

公开(公告)号：DE2621829A1

公开(公告)日：1976-11-25

申请号：DE2621829

申请日：1976-05-17

Applicant: ICI LTD

Inventor： PORTER KENNETH

IPC: D06M17/00 ,  B29C65/08 ,  D04H1/485 ,  D04H1/54 ,  D04H1/541 ,  D04H1/549 ,  D04H1/55 ,  D04H1/555 ,  D06B1/10 ,  D06B11/00 ,  D06M23/00 ,  D06P5/00 ,  D06P5/24 ,  B41M5/26

Abstract: Method for bonding fabrics based on distributed fusible thermoplastic material, characterized in that a transfer sheet carrying an ink comprising thermally transferable dye is contacted with the fabric; the sheet and the fabric are subjected to heat and pressure in separate areas, whereby the thermoplastic material becomes adhesive and binds the fabric, and the dye is also transferred on the fabric at least in areas corresponding to the separated areas. (Machine-translation by Google Translate, not legally binding)

公开(公告)号：DE1720952A1

公开(公告)日：1972-04-27

申请号：DE1720952

申请日：1967-04-21

Applicant: ICI LTD

Inventor： PORTER KENNETH

IPC: C08G63/78 ,  C08G17/01

Abstract: Fibre- and film-forming polyesters are made by polycondensing a bis glycol ester of a dicarboxylic acid or an oligomer thereof, at least part of the polycondensation reaction being carried out while the reaction mixture in liquid state is caused to move along a long narrow tube in a state of turbanular flow by continuous concurrent movement past the liquid of an inert gaseous fluid, the rate of flow of the gaseous fluid being such as to ensure that during at least part of the residence time of the reaction mixture in the tube the partial pressure of glycol in the gaseous fluid is below the equilibrium partial pressure for the reaction mixture with which it is in contact. Suitable glycols are bis-1:4-hydroxymethylcyclohexane and those of formula HO.(CH2)n.OH where n is 2 to 10. Suitable dicarboxylic acids are terephthalic acid and bis-1:2-(p-carboxyphenoxy)ethane. Suitable gaseous fluids are nitrogen and trichlorofluoromethane. The gaseous fluid may contain a substance which reacts with carboxyl end groups, e.g. ethylene oxide or diazomethane. The reaction mixture may be fed to the tube in liquid form or dispersed in a suitable liquid. In the case where the gaseous liquid may be liquefied, the same liquid may be used as that in which the reactants are dispersed. The tube may be of uniform bore or the bore may increase progressively towards the outlet. The gaseous fluid may be injected at one point or more than one point. In examples, poly-(ethylene terephthalate) oligomers were fed to a tube the first stage of which was 15 metres long and 2.4 mms. internal diameter and the second stage of which was 7.5 metres long and 6.6 mms. internal diameter, the oligomers being (a) dispersed in trichlorotrifluoromethane, (b) dispersed in trichlorotrifluoromethane and a eutectic mixture of diphenyl and diphenyl oxide and (c) in molten form, nitrogen being used as the gaseous fluid.