Process for preparing rigid foamed materials containing...

Details Process for preparing rigid foamed materials containing... Process for preparing rigid foamed materials containing...

1998-06-04

2003-01-21

Foelak, Morton (Department: 1711)

Synthetic resins or natural rubbers -- part of the class 520 ser

Synthetic resins

Cellular products or processes of preparing a cellular...

C521S167000

Reexamination Certificate

active

06509387

ABSTRACT:

It is known to blow polyurethane rigid foamed plastics, using low-boiling alkanes. It is advantageous to use cyclic alkanes for this purpose since, owing to their low thermal conductivity in the gaseous state, they greatly improve the thermal conductivity of the foamed plastic. The main substance used is cyclopentane. Cyclopentane, however, owing to its relatively high boiling-point (49° C.), has the disadvantage that it condenses at low temperatures, which occur normally when polyurethane rigid foamed plastic is used as an insulating material in domestic refrigerators. At these low temperatures, especially when used in refrigerators, cyclopentane does not have its full insulating effect, and also the undesired condensation of the blowing agent results in a negative pressure in the cell, which has to be compensated by increasing the rigidity of the foam or increasing the bulk density.
The object of the invention is to provide cyclopentane-containing blowing-agent mixtures which retain the good thermal insulation of cyclopentane even at low temperatures.
It has now surprisingly been found that by adding small proportions of low-boiling alkanes in the C
3
and C
4
series, the advantageous thermal conductivity of cyclopentane foam can be retained and also the pressure inside the cells can be considerably increased, especially at low temperatures. “Low temperatures” as usual means temperatures below 10° C., e.g. between −30° C. and +5° C.
An important feature of blowing-agent mixtures is that they are liquid at room temperature and the normally gaseous C
3
and C
4
components do not increase the vapour pressure of the total mixture above 1 bar. This has been found particularly in the case of mixtures of cyclopentane and n-butane and/or isobutane, so that no complications result in polyurethane processing. An admixture of low-boiling alkanes appreciably impairs the insulating effect but, at proportions of 10 to 25% by weight, the impairment is surprisingly small. Cyclopentane usually dissolves easily in most polyols used in rigid polyurethane foam. Low-boiling aliphatic alkanes have much worse solubility, so that C
3
and C
4
-alkanes added to cyclopentane reduce the solubility of the blowing agent. In this case it is advantageous to use polyols started on aromatic amines; these have excellent solubility even in the case of acyclic alkanes.
The invention accordingly provides a method of producing rigid foamed plastics containing urethane and optionally containing isocyanurate groups, by reaction of polyols, polyisocyanates, blowing agents and optional foam auxiliary substances, characterised in that the blowing agent is a mixture of 5 to 50 parts by weight of C
3
and/or C
4
alkanes and 50 to 95 parts by weight of cyclopentane.
The polyols and polyisocyanates in the method according to the invention can be any per se known starting components.
The isocyanate components can e.g. be aromatic polyisocyanates such as described by W. Siefken in Justus Liebigs Annalen der Chemie, 562, pages 75 to 136, e.g. substances having the formula
Q(NCO)
n
in which
n is 2 to 4, preferably 2, and
Q denotes an aliphatic hydrocarbon radical with 2 to 18, preferably 6 to 10 carbon atoms, or a cycloaliphatic hydrocarbon radical with 4 to 15, preferably 5 to 10 carbon atoms, or an aromatic hydrocarbon radical with 6 to 15, preferably 6 to 13 carbon atoms or an araliphatic hydrocarbon radical with 8 to 15, preferably 8 to 13 carbon atoms, e.g. polyisocyanates such as described in DE-OS 28 32 253, pages 10 to 11.
Particular preference as a rule is given to polyisocyanates which are easily obtainable industrially, e.g. 2,4 and 2,6-toluylene diisocyanate or any mixtures of these isomers (“TDI”), or polyphenyl polymethylene polyisocyanates produced by condensation of aniline and formaldehyde and subsequent phosgenation (“crude MDI”) or polyisocyanates containing carbodiimide groups, urethane groups, allophanate groups, isocyanurate groups, urea groups or biuret groups (“modified polyisocyanates”), more particularly modified polyisocyanates derived from 2,4 or 2,6-toluylene diisocyanate or from 4,4′- and/or 2,4′-diphenyl methane diisocyanate.
The starting components for the polyol component are compounds containing at least two hydrogen atoms capable of reacting with isocyanates and having a molecular weight usually between 62 and 20000. These include compounds containing amino groups, thiol groups or carboxyl groups and also and preferably compounds containing hydroxyl groups, preferably polyethers, polyesters, polycarbonates, polylactones and polyamides, particularly compounds containing 2 to 8 hydroxyl groups, especially those having a molecular weight of 1,000 to 20,000, e.g. compounds containing at least 2, usually 2 to 8, preferably 2 to 4 hydroxyl groups as known per se in the production of polyurethanes and described e.g. in DE-OS 28 32 253, pages 11 to 18. Mixtures of various compounds of this kind can also be used according to the invention.
Optionally, known additives and auxiliary substances, such as flame retardants, catalysts and foam stabilizers, are also used.
The flame retardants are per se known flame retardants, preferably products liquid at 20° C.
The foam stabilizers are preferably polyether siloxanes, especially if soluble in water. These compounds usually have a structure in which a copolymer of ethylene oxide and propylene oxide is combined with a polydimethyl siloxane radical. Foam stabilizers of this kind are described e.g. in U.S. Pat. Nos. 2,834,748, 2,917,480 and 3,629,308. The catalysts can be those known per se in polyurethane chemistry, such as tert.-amines and/or organometallic compounds.
Use can also be made of reaction retarders, e.g. acid-reacting substances such as hydrochloric acid or organic acid halides, or cell regulators of per se known kind such as paraffins or fatty alcohols or dimethyl polysiloxanes, or pigments or dyes, or stabilizers against ageing and weathering, plasticizers, fungistatic substances and bacteriostats or fillers such as barium sulphate, kieselguhr, carbon black or whiting.
Other examples of surface-active additives and foam stabilizers optionally also used according to the invention, cell regulators, reaction retarders, stabilizers, flame-retarding substances, dyes, fillers, fungistatic substances and bacteriostats and details about use and operation of these auxiliary substances are described in Kunststoff-Handbuch, Volume VII, published by Vieweg and Höchtlen, Carl Hanser Verlag, Munich 1966, e.g. on pages 121 to 205.
In the production of foam according to the invention, foaming can also be brought about in closed moulds. The reaction mixture is placed in a mould, which can be made of metal e.g. aluminium or plastic e.g. epoxy resin. In the mould, the expandible reaction mixture foams and forms the moulded member. The foaming process in the mould can be managed so that the moulded part has a cellular surface structure. Alternatively it can be managed so that the moulded part has a compact skin and a cellular core. The procedure according to the invention in the first case is to introduce expandible reaction mixture into the mould in an amount sufficient for the resulting foamed plastic just to fill the mould. In the latter case, the amount of reaction mixture introduced into the mould is more than enough to fill the interior of the mould with foamed plastic. In the latter case, operation is by “over-charging”. A method of this kind is known e.g. from U.S. Pat. Nos. 3,178,490 and 3,182,104.
The C
3
and/or C
4
alkanes used according to the invention are preferably n-butane and/or isobutane.
0.5 to 4 parts by weight of water can advantageously be used as a co-blowing agent in addition to the alkane mixture according to the invention. It is preferable to use 1.5 to 3 parts by weight of water as the co-blowing agent.
Preferably, in the production of rigid polyurethane foamed plastics according to the invention, the polyol component is a mixture of 5 to 80 parts by weight of polyol based on aromatic amines. It is particular

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