Use of polyether-polyurethane for safety clothing

Details Use of polyether-polyurethane for safety clothing Use of polyether-polyurethane for safety clothing

1999-05-17

2003-02-18

Sergent, Rabon (Department: 1711)

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

Synthetic resins

Cellular products or processes of preparing a cellular...

C036S02500A, C036S028000, C036S03200A, C521S051000, C521S137000, C521S174000, C521S176000, C521S172000, C521S173000, C525S123000, C525S127000, C525S131000, C525S453000, C525S455000, C525S460000, C528S060000, C528S066000, C528S076000, C528S077000, C528S080000

Reexamination Certificate

active

06521676

ABSTRACT:

This invention relates to the use of cellular to solid moulded plastics made from polyether PUR for the production of safety clothing, preferably safety shoe soles.
The production of moulded polyurethane-based plastics has been known prior art for many decades. These moulded plastics may be produced in a wide range of densities and hardnesses for various applications, for example as protective clothing.
The principal application for polyurethanes in safety clothing is as protective shoes. On the basis of existing standards (the EN 344 series), which lay down the structure and properties of safety shoes, the selection of materials has hitherto been restricted to the use of polyester PUR. The principal reason for excluding polyether PUR is its inadequate resistance to oil and petrol (EN 344, point 4.8.9, resistance to fuel).
However, polyester PUR or the components required for the production thereof by reaction injection moulding exhibit the following disadvantages:
elevated viscosities of the components in the ready-to-process state results in unfavourable reproduction of shapes
the elevated temperature of the components in the ready-to-process state, which is necessary for processing, reduces, their pot life
unsatisfactory resistance to hydrolysis and microbial attack, especially in agricultural use or in areas with a hot and humid climate, which also results in a restricted storage life of finished safety shoes
poor low temperature flexibility of standard polyester PUR
The production of polyether PUR using the reaction casting process or reaction injection moulding process, like polyester PUR processing, is part of the prior art. Depending upon requirements, polyester PUR is used at various densities and hardnesses in both single and double layer moulded sole and direct soling processes for the production of walking, leisure and sports shoes.
In connection with new developments of polyether-based PUR, such a PUR has surprisingly been found which exhibits sufficient fuel resistance for use in safety shoe applications.
The present invention provides the use of cellular to solid moulded polyether-based plastics by foam moulding to produce safety clothing.
Safety clothing complying with EN 344 series standards (fuel resistance in isooctane <12 vol. %) are, for example, safety shoes, boots, aprons etc..
This fuel resistance is achieved at outsole bulk densities of ≧800 kg/m
3
with the polyester PUR system raw materials stated below by way of example.
The cellular to solid polyether polyurethane based moulded plastics are produced by foam moulding a reaction mixture prepared, for example, from
a) a relatively high molecular weight polyether polyol component,
b) a polyisocyanate component
c) chain extenders,
d) optionally blowing agents,
e) activators and optionally
f) further auxiliary substances and additives,
wherein the starting materials are reacted while maintaining an isocyanate index of 70 to 130.
The relatively high molecular weight polyether polyol component a) has a hydroxyl functionality of 2.00 or substantially comprises a mixture having an average hydroxyl functionality of 2.02 to 2.95 prepared from
aa) at least one polyether diol of the hydroxyl value range from 10 to 115, which was produced by propoxylating a difunctional starter and subsequently ethoxylating the propoxylation product while maintaining a weight ratio of propylene oxide to ethylene oxide of 60:40 to 85:15 and
ab) at least one polyether triol of the hydroxyl value range from 12 to 56, optionally containing fillers based on styrene/acrylonitrile copolymers, polyureas or polyhydrazocarbonamides in a quantity of up to 20 wt. %, relative to the total weight of component a), which polyether triol was produced by propoxylating a trifunctional starter and subsequently maintaining a weight ratio of propylene oxide to ethylene oxide of 60:40 to 85:15.
Polyisocyanate component b) is a semi-prepolymer containing isocyanate groups and having an NCO content of 10 to 25 wt. %, produced by reacting (i) 4,4′-diisocyanato-diphenylmethane with (ii) a polyether component of the hydroxyl value range of 10 to 115 and an (average) hydroxyl functionality of 2.0 to 2.5, consisting of at least one polyether diol, produced by propoxylating a difunctional starter and optionally subsequently ethoxylating the propoxylation product using up to 40 wt. % of ethylene oxide, relative to the weight of the polyether diol, or a mixture of at least one such diol with at least one polyether triol, produced by propoxylating a trifunctional starter and optionally subsequently ethoxylating the propoxylation product using up to 40 wt. % of ethylene oxide, relative to the weight of the polyether triol and/or a polyester component of the hydroxyl value range from 28 to 115 and an average functionality of 2.0 to 2.5, wherein component (i) was optionally added before the reaction or to the reaction product with polypropylene glycols of the molecular weight range from 134 to 700 and/or by carbodiimidising a proportion of the isocyanate groups of liquefied 4,4′-diisocycanatodiphenylmethane in a quantity of up to 10 wt. %, relative to the weight of component (i).
1,2-Ethanediol and/or 1,4-butanediol and/or diethylene glycol and/or triethanolamine and/or diethyltolylenediamine are used as component c),
while water and/or a physical blowing agent, for example R 134a® (hydrofluoro-alkane mixture), are optionally used as component d).
Activators e) which may be considered are the compounds known per se from polyurethane chemistry, such as for example triethylenediamine, N,N-dimethyl-benzylamine or organotin compounds, such as for example dibutyltin dilaurate or tin(II) octoate.
Further optionally used auxiliary substances and, additives f) which may be mentioned by way of example are surface-active substances, foam stabilisers, cell regulators, internal release agents, dyes, pigments, hydrolysis stabilisers, fungistatically and bacteriostatically active substances, light stabilisers, anti-oxidants and anti-static agents (quaternary ammonium compounds).
The polyurethanes are produced in accordance with the known prior art. This means in general that components a) and c) to f) are combined to produce a “polyol component” and reacted in a single stage with the polyisocyanate component b) in a closed mould, for example a closed metal or plastic mould, wherein conventional two-component mixing units are used. The quantity of the reaction mixture introduced into the mould and the quantity of the water optionally used as the blowing agent and/or of a physical blowing agent, for example R 134®, are calculated in this process in such a manner that moulded foams of a bulk density of ≧800 kg/m
3
are obtained. The most important area of application is in shoe production, according to the invention for the production of cellular to solid outsoles for safety shoes. These shoes preferably have an outsole bulk density of ≧800 kg/m
3
and, in a particular embodiment, are associated with a throughsole having a bulk density of ≧400 kg/m
3
.


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