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Description  |
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Water-soluble air-drying alkyd resins have long been known. According to
French Pat. Specification No. 1,369,013, for example, they can be produced
by reacting alkyd resins with quantities of anhydrides of polybasic
carboxylic acids such that resins with acid numbers of more than 50 are
formed. Although resins of this kind can also be air-drying, it is
regarded as better, in view of their high acid numbers, to produce
melamine-resin-crosslinking stoving lacquers from them (page 3, left-hand
column, paragraph 3).
German Offenlegungsschrift No. 1,916,972 describes water-soluble,
air-drying polyurethane resins which are distinguished by the fact that
they are isocyanate-extended, fatty-acid-modified low molecular weight
polyols. This variation is said to improve the bond strength of air-drying
systems (page 10, paragraph 2). A complicated production process,
comprising in all at least three different stages, is required to obtain
this result, because first of all a preliminary product has to be
produced, and the resulting resin must subsequently be extended with
isocyanates and finally reacted with anhydrides. To obtain further
improvement, modification with oil-reactive phenolic resins, such as butyl
phenol resols, is also regarded as necessary, involving another process
stage (cf. page 6, paragraph 3, and page 7, paragraphs 2 and 3). The
polyurethane resins thus obtained increase the water up take of
conventional alkyd resin systems (page 11, paragraph 2). In the case of
mixtures of this kind with conventional alkyd resins, this can be a
valuable property for lacquering spray-moist substrates, although in cases
where binders of this kind are used as sole binders, this hydrophilic
character is more of a disadvantage for protecting the substrate.
On the other hand, fully condensed alkyd resins have also been further
extended through polyisocyanates in another process stage, and semiesters
subsequently produced in order to obtain better air-drying systems (German
Offenlegungsschrift No. 1,917,162).
Unfortunately, this measure is attended by the disadvantage that a reaction
with isocyanates which is hard to carry out and difficult to keep
consistent is again required for obtaining waterproof coatings.
Finally, when the changeover was made to short-oil water-soluble alkyd
resins, it was found to be necessary, in addition to the isocyanate
modification, to modify the fatty acids by reaction with phenolic resins,
again with the object of improving the resistance to water of systems of
this kind (Belgian Pat. No. 803,346).
It was therefore particularly surprising and by no means foreseeable that
it should also be possible, by a particularly simple reaction involving
only two stages, without any need for further complicated urethane
modification, to obtain binders which yield thoroughly drying waterproof
lacquer compositions with great reproducibility.
Accordingly, the present invention relates to a process for the production
of water-dilutable binders based on air-drying short-oil alkyd resins
acidified by semiester formation with dicarboxylic acid anhydrides which
alkyd resins have acid numbers of from 30 to 70, preferably from 42 to 48,
and hydroxyl numbers of from 40 to 120 and a content of natural
unsaturated fatty acids in an amount of from 15 to 50, preferably 20 to
34% by weight and of a co-condensed natural-resin-modified phenol resol
resin in an amount of from 2 to 10% by weight, characterised in that (1)
the molar composition of the alkyd resin before semiester formation
corresponds to a polyalcohol/polycarboxylic acid
(anhydride)/monocarboxylic acid ratio of 1:(0.5- 1):(0.3- 1), and (2)
polyalcohols, polycarboxylic acids resp. their anhydrides, monocarboxylic
acids and phenolic resins are co-condensed in a single process stage,
followed only by semiester formation with dicarboxylic acid anhydrides.
By alkyd resins there are to be understood polycondensates produced by
polycondensation of alcohols and carboxylic acids according to known
methods of the kind defined in Rompp's Chemielexikon, Vol. 1, page 202,
Franckh'sche Verlagsbuchhandlung Stuttgart, 1966 or described, for
example, by D. H. Solomon, The Chemistry of Organic Film Formers, pages
75-101, J. Wiley & Sons Inc., New Yor, 1967.
Polyalcohols suitable for the preparation of the alkyd resins are
aliphatic, cycloaliphatic and/or aromatic alcohols containing 1 to 6,
preferably 1 to 4, hydroxyl groups attached to non-aromatic carbon atoms,
glycols such as ethylene glycol, propylene glycol, butane diols; ether
alcohols such as diethylene and triethylene glycols; oxethylated
bisphenols, perhydrogenated bisphenols; trimethylolethane,
trimethylolpropane, glycerol, pentaerythritol, dipentaerythritol, mannitol
and sorbitol.
Acid components suitable for the preparation of the alkyd resins are
aliphatic, cycloaliphatic saturated or unsaturated and/or aromatic
polybasic carboxylic acids, preferably di-, tri- and tetrabasic carboxylic
acids containing 4 to 12 carbon atoms per molecule and the esterificable
derivatives thereof (e.g. anhydrides or esters) e.g. phthalic acid
anhydride, isophthalic acid, terephthalic acid, tetrahydro- and
hexahydrophthalic acid anhydride, trimellitic acid anhydride, pyromellitic
acid anhydride, maleic acid anhydride, adipic acid and succinic acid as
well as halogenated acids such as chlorophthalic acid and Het acid.
Monocarboxylic acids suitable for the preparation of the alkyd resins are
aliphatic, cycloaliphatic saturated and unsaturated and/or aromatic
monocarboxylic acids containing 6 to 24 carbon atoms per molecule such as
benzoic acid, butylbenzoic acid, tolyl acid, hexahydrobenzoic acid,
abietic acid as well as unsaturated natural fatty acids and esters thereof
such as linseed oil, soya bean oil, wood oil, safflower oil, dehydrated
castor oil and castor oil, cotton seed oil, ground nut oil, tall oil fatty
acids, linseed oil fatty acid, the fatty acids of soya bean oil, of wood
oil, of safflower oil and of castor oil and dehydrated castor oil and
products obtained from natural unsaturated oils or fatty acids by
conjugation on isomerisation. Suitable saturated fatty acids are, for
example, coconut oil and .alpha.-ethylhexanoic acid.
The molecular weight destined as number average of the alkyd resins is from
1000 to 10,000, preferably from 1000 to 5000 (molecular weights below 5000
destined by vapour pressure osmosis in dioxane and acetone; if both values
differ from each other the lower value is considered to be the more
accurate one; molecular weights above 5000 destined by membrane osmosis in
acetone).
Suitable natural-resin-modified phenolic resins are the reaction products
of colophony and resols, optionally esterified with polyalcohols, which
are known in the literature as Albertol. Resols are the phenolic resins
which can be produced under acid conditions from phenol and formaldehyde
(Hultzsch, Chemie der Phenolharze, Springer-Verlag 1960, pages 157 et
seq).
Dicarboxylic acid anhydrides suitable for semiester formation are, for
example, phthalic acid anhydride, succinic acid anhydride, maleic acid
anhydride and preferably, tetrahydrophthalic acid anhydride.
Production is carried out exclusively on the simplified production
principle of direct co-condensation with stirring in an inert gas
atmosphere, of polyalcohols, carboxylic acids and phenol derivatives at
reaction temperatures generally in the range of from 180.degree. to
270.degree. C., preferably in the range of from 240.degree. to 250.degree.
C. and more especially at a reaction temperature of 260.degree. C. It may
be assumed that the phenolic resin portions do not take part exclusively
in the polycondensation reaction, but also interact through addition
reactions with the double bonds of the unsaturated fatty acids. Reactions
of this kind take place in accordance with the following model equations:
##STR1##
wherein R.sup.1 = radical of a natural-resin-modified phenolic resin
R.sup.2 = aliphatic radical
R.sup.3 = aliphatic radical
A= alkyd resin radical (A--OH= alkyd resin)
Chromane ring systems of this kind are then constituents, attached by
condensation through carbon bonds, in the drying alkyd resin coating.
On completion of the reaction, the reaction mixture is normally cooled and
the semiester is formed in the cooling phase at about 160.degree. to
120.degree. C. by the addition of a dicarboxylic acid anhydride,
preferably tetrahydrophthalic acid anhydride.
The free acid groups of the alkyd resins are usually completely neutralised
by inorganic or organic bases. In many cases, however, the alkyd resins
are sufficiently water-soluble if neutralised in an amount of 70 to 80%.
Suitable bases are for example, ammonia, primary secondary and tertiary
amines such as ethylamine, diethylamine, triethylamine,
dimethylethanolamine, mono-, di- and triethanolamine,
dimethylaminopropanol, and optionally alkali hydroxides.
The alkyd resins obtained according to the process of the invention which
have been partly or completely neutralised can be mixed with
water-dilutable organic auxiliary solvents such as, for example,
monohydric alcohols such as ethanol, iso-propanol, butanols;
ethyleneglycol monoalkyl esters such as ethyleneglycol monomethyl,
monoethyl and monobutyl ether, ketones such as acetone, methyl ethyl
ketone; ketoalcohols and cyclic alkyl ethers such as tetrahydrofurane.
The binders obtained according to the process of the invention are
extremely suitable as basis for primers protecting varnishes for metal
surfaces. for metal surfaces.
The invention is illustrated by but by no means limited to the following
Examples, in which the parts and percentages quoted are parts and
percentages by weight.
EXAMPLE 1
An alkyd resin is produced from 1667 parts of linseed oil, 425 parts of
pentaerythritol, 1000 parts of trimethylol propane, 185 parts of linseed
oil fatty acid, 457 parts of benzoic acid, 1201 parts of phthalic acid
anhydride and 15 parts of a natural-resin-modified phenolic resin having a
melting range of from 118.degree. to 130.degree. C. and an acid number of
less than 20 (trade name Albertol 626L, product of the firm of Hoechst AG,
Werk Albert), by polycondensation at 260.degree. C. until a resin with a
viscosity corresponding to a time of outflow of 88 sec (70% in dimethyl
formamide, destined according to DIN 53 211) is formed. The resin thus
formed is subsequently converted into a polysemiester with an acid number
of 45 by the addition of 464 parts of tetrahydrophthalic acid anhydride at
130.degree. C. This alkyd resin with an oil content of 30% and a phenolic
resin content of 2.8% is dissolved to form an 88% solution in ethylene
glycol monobutyl ether, followed by the preparation of a water-dilutable
commercial form of this solution. It has the following composition:
finally
124.5 parts of the 88% solution,
5.0 parts of ethyl glycol,
45.0 parts of isopropanol,
8.8 parts of triethyl amine, and
16.7 parts of water.
A clear lacquer with the following recipe is prepared from this solution
which has a binder content of 55%: 53.90 parts of the 55% commercial form,
44.90 parts of water, and 1.20 parts of Co-Pb-Mn-naphthenate solution (1:2
in xylene with a metal content of 1.5% of Co, 22% of Pb, 1.5% of Mn)
100.00 parts.
Lacquers containing these binders show favourable drying behaviour, dry out
thoroughly and give surprisingly waterproof elastic lacquer coatings of
high bond strength.
EXAMPLE 2
The lacquers mentioned in the following Table were tested as clear lacquers
in accordance with Example 1. The drying test on glass plates produced the
following results:
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Isocyanate-
and phenolic
Isocyanate-
resin-
Binder modified
modified
according
binder acco-
alkyd resin
to the invention
rding to DT-
according to
Binder (Example 1)
OS, 1,917,162
BE-PS 803,346
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oil content 30 % 50 % 24%
drying time in hours
7 h 5.5 h 5 h
at room temperature
complete drying
O- O- 0
after 24 hours
water resistance after
1 h without
1.5 h with-
1 h with-
24 hours any change
out any
out any
wad test change change
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The Comparison Test shows that, even in the absence of the isocyanate
modification which necessitates additional process stages, it is possible
to obtain valuable water-dilutable lacquers which give good lacquer
finishes. Accordingly, the Examples corresponding to the closest prior art
were selected from the known patent literature. The differences in
individual values are attributable to the fact that comparable binders
with the same oil contents were not described as Examples in every case.
The Comparison Test with the isocyanate-modified or isocyanate-and
phenolic-resin-modified alkyd resins produced by the multistage process
shows that it is possible, by using the more easily produced
isocyanate-free phenolic-resin-modified alkyd resins according to the
invention, to obtain equivalent lacquer finishes, even without isocyanate
modification, by keeping to the process stages according to the invention.
* * * * *
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Description  |
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