Patent Application
20100216926
The present invention is related to the area of lacquers and paint additives and concerns the use of glycerol acetals as green solvents, in particular coalescent agents for said products.
The quality of an optimum decorative paint results from a number of components performance that is a part of such formulation. Each element, each raw material is present to impart properties and characteristics to contribute with and modify the results of the final product quality. Certainly, a proper choice may change for example the hiding power, gloss, drying, durability, and including, the cost.
Among the main raw materials that sensitively impact the quality of a basic formulation in decorative paints one finds the coalescent agents. By definition, coalescence means the process through which a cell or latex particle (high molecular weight polymers dispersed in water) approaches themselves, agglutinate, and fuse to build a continued and homogeneous film. After the first step, the evaporation, and under room temperature, some paints can even decrease the film forming temperature (Tg—vitreous transition temperature) and build the expected film with no use of any coalescent. The result, however is extremely soft films that become dirty easily, are hard to be cleaned, and are very little resistant and durable. However, adding a coalescent even under adverse conditions such as low temperatures, high humidity, leads to high quality and performance films. A general and detailed description of the coalescent effect can be found in H. J. Kok, Filmbildehilfsmittel, in: H. Kittel (ed.) Lehrbuch der Lacke and Beschichtungen, 2. Edition., Bd. 4, Hrsg. M. Ortelt, S. Hirzel Verl., Stuttgart (2007).
Taking the disadvantages of the state of the art into account it has been the object of the represent invention to provide new coalescent agents/solvents for making lacquers and paints which show compared to the products found in the market
The present invention refers to the use of glycerol acetals as coalescent agents and/or solvents for making lacquers and paints.
Surprisingly it has been observed that acetals made from glycerol, in particular glycerol isobutyral meet all the criteria of the profile explained above. Replacing coalescent agents found in the market, as for example butyl glycol or trimethyl butyrate, by the acetals according to the inventions, similar behaviour of the MFFT has been found The films show improved hardness, scrub and block resistance and gloss, also at lower additive concentrations. One can also observe that the gloss of the films are stable even if exposed to higher temperatures over longer periods of time, e.g. 3 days at 60° C. Finally, as example isobutyral acetal shows a biodegradability level of 78, therefore it is considered readily biodegradable
Glycerol acetals may be derived from all kinds of aliphatic or aromatic aldehydes referring to general formula (I),
R1—COH (I)
in which R1 stands for a linear or branched, saturated or unsaturated aliphatic alkyl radical having 1 to 22, preferably 2 to 6 carbon atoms, or an aromatic ring having 5 to 12, preferably 5 or 6 carbon atoms, optionally containing nitrogen or oxygen atoms replacing one or two carbon atoms in the ring system, and also optionally substituted by one or more hydroxy groups. Examples for suitable aldehydes forming the starting material for the glycerol acetals encompass propianaldehyde, pentanal, isoamylaldehyde, octanal, 2-methylhexyl aldehyde, nonanal, dodecanal, isotridecanal, hexadecanal and octadecanal. The preferred glycerol acetals are those derived from isobutyraldehyde, 2-ethylhexyl aldehyde, furfuryl aldehyde and benzaldehyde having the following formulae:
A preferred process for obtaining the glycerol acetals to be used according to the present invention comprises the following essential steps:
More particularly, the preferred process for the production of said glycerol acetals is encompasses the reaction of glycerol with one or more of said aldehydes in the absence of organic solvents and in the presence of phosphoric acid as catalyst, the molar ratio of glycerol to aldehyde(s) being adjusted to a value of 1:1 to 1:1.2. In order to avoid ambiguities, it is pointed out that, where the molar ratio of glycerol to aldehydes is mentioned, the singular form “aldehyde” refers to the fact that either a single aldehyde is used while the plural form “aldehydes” refers to the fact that one or more aldehydes is/are used. Accordingly, the glycerol to aldehyde ratio is always understood to be the molar ratio of glycerol to the totality of aldehyde(s). According to the process as described above acetals are obtained in a high yield (at least 95%, based on the glycerol used) showing a gas-chromatographic purity of at least 95% (percentage area GC) without any need for special purification steps, such as filtration or additional distillation. In addition, the products obtained are colourless. The molar ratio of glycerol to aldehydes is preferably adjusted to a value of ca. 1:1.1. Glycerol may be used in pure form or with a water content of up to 20% by weight in the process according to the invention. Water-containing glycerols are available, for example, from the biodiesel process. The process is distinguished by short to moderate reaction times. A time of 3 to 6 hours is generally sufficient for a substantially quantitative conversion. The catalyst used (phosphoric acid) is preferably used in a quantity of 0.1 to 0.8 mol-% (and preferably in a quantity of 0.2 to 0.6 mol-%), based on glycerol. The reaction is typically conducted at temperatures of 40 to 150° C. and preferably at temperatures of 70 to 130° C. In one embodiment, the water of reaction is continuously removed from the reaction mixture, preferably using an apparatus of the Dean Stark type. The reaction is preferably carried out in an inert gas atmosphere, for example under nitrogen. Following this manufacturing routine, the 5- and 6-rings of the particular corresponding acetals (see the above formulae) accumulate in a ratio of ca. 80:20.
The glycerol acetals have been found useful as coalescent agents for making lacquers and paints to which they typically are added in amounts of from 0.1 to 10, preferably 0.5 to 5 and more preferably 1 to 2% b.w. —calculated on the final composition.
Another object of the present invention relates to lacquers or paints, comprising
In addition the products may also contain antifoaming agents, thickening agents and/or associative thickeners, dispersing agents, humectants, organic solvents and the like. More particularly, the products may comprise
The preferred pigment for making lacquers and paints is of course titanium dioxide, however; also all kinds of organic or inorganic pigments as for example compiled in Lacke and Druck-farben, U. Zorl, Hrsg., Georg Thieme Verl., Stuttgart, N.Y. (1998) can be incorporated into the products. In a preferred embodiment said dyes are encapsulated for example—but not limited to—in a shell formed from anionic and/or cationic polymers or proteins. Among the resins a base formed from acrylic/styrenic copolymers is typical. Preferred filler is calcium carbonate. The paints according to the present invention may be gloss paints, semi-gloss paints or flat paints.
A 50-liter multipurpose reactor equipped with a mechanical stirrer and distillation head with a water separator and nitrogen inlet was charged under nitrogen at 20° C. with 10,195 g (110.8 mol) glycerol, 40.0 g (0.35 mol) phosphoric acid (85% in water) and 9,445 g (131 mol) isobutyraldehyde (the main object of the excess was to fill the dead space in the water separator). The temperature was increased to 130° C. in 3 hours. During the reaction, the water of reaction formed was continuously removed. The reaction was terminated after 2 hours at 130° C. Excess isobutyraldehyde was discharged with a stream of nitrogen, 730 g isobutyraldehyde being recovered. The quantity of water removed amounted to 2200 g. The target product (glycerol acetal of isobutyraldehyde) was obtained in a yield of 16,720 g (=97% of theory) showing an APHA colour of 30.
The minimum film forming temperature has been determined by adding up to 2% b.w. of glycerol isobutyral or a standard coalescent agent (TMB=trimethyl butyrate) to a standard styrene acrylic composition. The results are compiled in table 1.
As one can see, the substitution of TMB by glycerol isobutyral shows similar MFFT behaviour and even lower MFFT at higher concentrations.
The pendulum hardness of various films has been determined according to the procedure described in DIN 53157/ASTM D 4366 by adding glycerol isobutyral or TMP at 1 or 2% b.w. (film thickness: 50 micron; styrene-acrylic emulsion with 50% b.w. solids contents). The results are compiled in Table 2:
Compared to the standard (TMB) the addition of glycerol isobutyral increases the pendulum hardness of the films also at lower concentrations right from the beginning of the film formation.
The scrub resistance of various films has been determined according to the procedure described in ASTM D2486 by adding glycerol isobutyral or TMB at 1% b.w. (tests conducted after 7 days from paint drying). Gloss was tested according to ISO 2813/ASTM D523. The results are compiled in Table 3:
A semi gloss paint (3% b.w. solvent, 38% b.w. resin content with 50% b.w. solids) and a flat paint (2% b.w. solvents, 10% resin content with 50% b.w. solids) were prepared using glycerol isobutyral (GIB) or butylglycol (BG) as coalescent agents/solvents. The results are compiles in Table 4:
Table 5 reflects a typical composition of a semi-gloss paint comprising glycerol isobutyral as a solvent/coalescent agent.
| Number | Date | Country | Kind |
|---|---|---|---|
| 07020568.7 | Oct 2007 | EP | regional |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP08/08620 | 10/11/2008 | WO | 00 | 4/20/2010 |
