Method for producing ready-to-use soft PVC films or profiles

Patent metadata

Field	Value
Publication number	US-10059814-B2
Application number	US-201515113579-A
Country	US
Kind code	B2
Filing date	Feb 12, 2015
Priority date	Feb 13, 2014
Publication date	Aug 28, 2018
Grant date	Aug 28, 2018

Abstract

The extrusion of polymer compositions based on polyvinyl chloride (PVC) and in particular to a method in which polymer compositions are produced that have an elongation at break of at least 200%, a tensile strength of at least 10 N/mm2 with a specific energy input SEI of 0.03 to 0.20 kWh/kg and in particular 0.04 to 0.16 kWh/kg. The method is expediently carried out such that a plasticizer is added in a plurality of portions to the non-composed polyvinyl chloride and mixed into said polyvinyl chloride. The method thereby offers a fast and simple possibility of producing products from finished soft PVC, the production of said products requiring only a single processing device in the form of an extruder.

First claim

The invention claimed is:

1. A method for extruding a homogeneous polymer composition, which has a degree of gelation of 60% to 100%, an elongation at break of at least 200%, and a tensile strength of at least 10 N/mm 2 , from an uncompounded polyvinyl chloride, wherein the quantity of energy introduced into the polymer composition within the method, as indicated by the specific energy input (SEI), is 0.03 to 0.20 kWh/kg.

2. The method as claimed in claim 1 , wherein the uncompounded polyvinyl chloride is polyvinyl chloride prepared by suspension polymerization.

3. The method as claimed in claim 1 , wherein said extrusion apparatus is a planetary roller extruder, an annular extruder, a multiscrew extruder or a Buss kneader.

4. The method as claimed in claim 1 , wherein the amount of energy introduced by the extrusion apparatus may be introduced both in the form of mechanical energy and in the form of thermal energy and that at the end of the extrusion apparatus a product temperature is reached of at least 150° C. up to at most 190° C.

5. The method as claimed in claim 1 , wherein the homogeneous polymer composition has a residual thermal stability, determined according to DIN 53 381-1 at 180° C., of at least 60 minutes.

6. The method as claimed in claim 1 , wherein the extrusion apparatus used for the extrusion comprises a pair of substantially isomorphous, elongate rotors which fit into the cavity and are disposed next to one another for interpenetrating movement.

7. The method as claimed in claim 6 , wherein each of the rotors has a length L in the range of 32-60 times its diameter D.

8. The method as claimed in claim 6 , wherein the polyvinyl chloride is admixed with a first portion of plasticizer at an L/D ratio in the range from 1 to 8 and with a second portion of plasticizer at an L/D ratio of 10 to 20.

9. The method as claimed in claim 1 , the polymer composition consisting substantially of
(A) 30 to 80 wt % of polyvinyl chloride,
(B) 0.5-5 wt % of a stabilizing additive,
(C) 0-40 wt % of a solid constituent, and
(D) 5-40 wt % of a plasticizer, liquid at room temperature, for the polyvinyl chloride,
where the figures in wt % are based in each case on the total weight of the polymer composition, and
where the method comprises the steps of
(I) feeding polyvinyl chloride (A) in uncompounded form into an extrusion apparatus having at least one rotor, which has at least three kneading and/or mixing zones and is capable of both transporting and mixing the mixture,
(II) feeding the polyvinyl chloride (A) and stabilizing additive (B) into the extrusion apparatus through a first inlet, which is disposed in the vicinity of the drive unit and adjacent to a first conveying segment section of the at least one rotor;
(III) feeding the plasticizer to the polyvinyl chloride mixed with the stabilizing additive through at least two inlets at a distance from one another, the plasticizer being added in at least two portions each of about 20-80 wt %, based on the total weight of the plasticizer, to the polyvinyl chloride, there being a kneading and/or mixing zone disposed between the addition of the individual portions,
(IV) working the plasticizer/polyvinyl chloride mixture at a temperature of or above the glass transition temperature of the polyvinyl chloride, the temperature of the mixture not exceeding 150° C., until the plasticizer has been incorporated substantially completely into the polyvinyl chloride,
(V) optionally feeding the solid constituent to the polyvinyl chloride mixed with the plasticizer in a section at which at least 80 wt % of the total amount of the plasticizer has been incorporated into the polyvinyl chloride,
(VI) optionally devolatilizing and extruding the mixture through the extrusion die.

10. The method as claimed in claim 9 , wherein the solid constituent is added to the polyvinyl chloride, mixed with the plasticizer, in a section at which at least 95 wt % of the plasticizer has been kneaded into the polyvinyl chloride.

11. The method as claimed in claim 9 , wherein the polyvinyl chloride is admixed in step (V) with at least 80 wt %.

12. The method as claimed in claim 9 , wherein the mixture of plasticizer and PVC is brought to a temperature of at least 30° C. below the glass transition temperature (Tg) of the polyvinyl chloride.

13. The method as claimed in claim 9 , wherein the amount of the solid constituent in the polymer composition is 0.01 to 35 wt %.

14. The method as claimed in claim 9 , wherein the solid constituent is incorporated into the polyvinyl chloride only after the plasticizer has been incorporated substantially completely into the polyvinyl chloride.

15. The method as claimed in claim 9 , wherein the individual portions for the feeding of the plasticizer to the polyvinyl chloride, mixed with the stabilizing additive, in step (III) account for about 30 to 70 wt % based on the total weight of the plasticizer.

16. The method as claimed in claim 15 , wherein the plasticizer is added in two portions to the polyvinyl chloride, with the portion added first making up 55±3 wt % and the portion added thereafter 45±3 wt % of the total amount of the plasticizer.

Assignees

• Sika Tech Ag

Inventors

• Wolf Ulrich
• Frei Fabian

Classifications

• B29C48/40

  using two or more parallel screws {or at least two parallel non-intermeshing screws}, e.g. twin screw extruders · CPC title

• B29C48/402

  the screws having intermeshing parts · CPC title

• C08J5/18

  Manufacture of films or sheets · CPC title

• B29K2027/06

  PVC, i.e. polyvinylchloride · CPC title

• C08K5/12

  of cyclic polycarboxylic acids · CPC title