AU3695189A - Creación de Inventos y Patentes con Inteligencia Artificial

AU3695189A – Thermoplastic molding compositions
– Google Patents

AU3695189A – Thermoplastic molding compositions
– Google Patents
Thermoplastic molding compositions

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Publication number
AU3695189A

AU3695189A
AU36951/89A
AU3695189A
AU3695189A
AU 3695189 A
AU3695189 A
AU 3695189A
AU 36951/89 A
AU36951/89 A
AU 36951/89A
AU 3695189 A
AU3695189 A
AU 3695189A
AU 3695189 A
AU3695189 A
AU 3695189A
Authority
AU
Australia
Prior art keywords
alkyl
value
grams
composition
reactant
Prior art date
1989-04-05
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)

Granted

Application number
AU36951/89A
Other versions

AU639207B2
(en

Inventor
Robert M. McCutchen Jr.
Anthony J O’lenick Jr.
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)

Solvay USA Inc

Original Assignee
GAF Chemicals Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
1989-04-05
Filing date
1989-05-10
Publication date
1990-11-05

1989-05-10
Application filed by GAF Chemicals Corp
filed
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GAF Chemicals Corp

1990-11-05
Publication of AU3695189A
publication
Critical
patent/AU3695189A/en

1993-07-22
Application granted
granted
Critical

1993-07-22
Publication of AU639207B2
publication
Critical
patent/AU639207B2/en

2000-03-09
Assigned to RHODIA INC.
reassignment
RHODIA INC.
Alteration of Name(s) in Register under S187
Assignors: RHONE-POULENC SURFACTANTS AND SPECIALTIES, L.P.

2009-05-10
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legal-status
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Status
Expired
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Classifications

C—CHEMISTRY; METALLURGY

C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON

C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients

C08K5/00—Use of organic ingredients

C08K5/04—Oxygen-containing compounds

C08K5/10—Esters; Ether-esters

C08K5/101—Esters; Ether-esters of monocarboxylic acids

C—CHEMISTRY; METALLURGY

C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON

C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients

C08K5/00—Use of organic ingredients

C08K5/04—Oxygen-containing compounds

C08K5/10—Esters; Ether-esters

C08K5/11—Esters; Ether-esters of acyclic polycarboxylic acids

Abstract

The invention relates to thermoplastic compositions containing an effective internal lubricating amount of a branched guerbet alcohol derived ester having the formula wherein R is hydrogen, -CO-alkyl or -CO-alkenyl; each R min is independently alkyl or alkenyl, said alkyl or alkenyl radicals having from 5 to 25 carbon atoms; each R sec is independently hydrogen, methyl or ethyl; m and n are each integers having a value of from 0 to 150; p is an integer having a value of from 4 to 12 and s is an integer having a value of from 2 to 36. The invention also relates to the molded or extruded product of said thermoplastic composition.

Description

THERMOPLASTIC MOLDING COMPOSITIONS
BACKGROUND OF THE INVENTION
Thermoplastic resins, as opposed to cross-linked thermosetting resins, possess a tendency to cloud and undergo discoloration under certain conditions. This effect is caused in part by polymeric decomposition when exposed to elevated temperatures, or contact with moistur or oxygen. Among the many thermoplastic resins, molded a extruded polycarbonate thermoplastics are in great demand due to their high resiliency, resistance to attack by chemical solvents, high heat stability, non-toxicity and clear, colorless film forming properties, many of which properties are lacking in thermosetting resins such as those disclosed in U.S. Patent 3,917,555.
High clarity and water-white color are particularly important characteristics in polycarbonate products which demand an exceptionally high degree of colorless transparency. Further, polycarbonates of high molecular weight are generally desired for hard, resilie transparent and colorless products such as bullet-proof safety glass, street light lenses, bottles, automotive light shields, kitchen appliances, safety glasses, packaging films and others. Clear, colorless polycarbon sheets are particularly desirable in applications where transmission of light is required, as in the lenses of automotive headlights. Prior polycarbonate lenses have tended to yellow with time. Accordingly, it has been th aim of research to develop a polycarbonate with eliminat or minimizes this disadvantage. In U.S. patent 4,431,67 there are disclosed certain cosmetic formulations containing certain guerbet alcohol derived esters. However, such cosmetic uses do not require colorless transparency in the final product. Exceptional uniformi

is also demanded for precision molded articles of high molecular weight polycarbonate thermoplastics used in laser read compact recording discs, microwave cookware and containers for comestible or medical products.
The thermoplastic moldable polycarbonates require special care in processing since many difficulties which are absent from thermosetting resins and which are unique to these resins are encountered. Notable among the difficulties in molding is the tendency of polycarbonates to degradation (i.e. discoloration and generation of carbon dioxide bubbles) in the presence of small amounts of water or methyl alcohol. It is also known that atmospheric oxygen is troublesome since it not only causes discoloration but also induces cross-linking, a condition to be avoided where resiliency and absence of color are required- (Encyclopedia of Chemical Technology, Kirk-Othmer, 2nd Edtion, Vol. 16 page 108). Thus, the kneading steps employed in U.S. patent 3,913,555 for thermosetting resins, and other operations which may introduce oxygen or moisture, are strictly prohibited. It has also been suggested that the pre.–ice of esters may be detrimental since certain species swell the polymer (Encyclopedia, Ibid) , tend to migrate to the polymer surface and cause stress -points which lead to cracking in molded sheets during storage.
Localized overheating of thermoplastic resins may occur- during the extrusion melting process wherein frictional forces generated within the extruder or other malaxing device are employed to melt the thermoplastic resin. he presence of a lubricating component such as mineral oil is previously known in the art to assist in polymer melt lubrication and reduction in thermoplastic polymer degradation.

In addition to the foregoing effects molten polycarbonate resins in particular are known to be relatively viscous. Such viscosity is affected by molecular weight and temperature, in the preparation of molded objects the reduced melt viscosity of a thermoplastic resin allows reduced molding cycle times thereby generating greater efficiency. Within design restraints it may be possible to attain decreased melt viscosity only by use of increased temperatures or reduced polymer molecular weight. The disadvantage in using elevated molding temperatures in increasing polymer degradation have been previously disclosed. Lower molecular weight polymers generally possess inferior strength properties, in particular, reduced impact and tensile properties. Accordingly there exist molding constraints which may prevent improved molding efficiency by either increased molding temperatures or reduced polyme molecular weight.
An improved internal lubricant may, however, also serve to reduce the melt viscosity of the molten resin in which it is incorporated allowing the successful molding higher molecular weight resins compared to resins lacking such lubricant or alternatively allowing reduced injectio molding times for resins of the same molecular weight. Ideally an improved internal lubricant for thermoplastic resins would possess desirable properties in both decreasing polymer degradation and reducing polymer melt viscosity.
Mold release additives perform the desirable function of permitting easy release of the molded object from the surface of the mold cavity after resolidificatio of the thermoplastic resin. Such additives are desirably incorporated into the polymeric resin itself, instead of being physically applied to the mold surface by the

operator. Such mold release additives are referred to in the art as internal mold release additives. Sometimes, but not always, a composition may act both as a lubricant for the polymer and as a mold release additive. Thus it cannot be determined a priori from the fact of a composition’s known lubricating ability that such composition also will possess good mold release properties. Not only must the composition be successful in reducing the force needed to remove the molded object from the mold, but the material must be compatible with thermoplastics and not cause polymer degradation especially at elevated temperatures. Also the composition should not cause deposition or plate out to occur on the mold surfaces (necessitating frequent mold cleaning) , and should not contaminate the surface of the resulting molded object. The latter property allows coextrusion to other thermoplastic resin layers or subsequent operations such as painting, laminating, etc. to be performed without first cleaning the surface of the molded object.
A further desirable feature of the foregoing additives is that the same be a liquid which allows ease of handling and incorporation into the thermoplastic resin.
Also, it would be desirable if there were provided a composition for use with thermoplastic molding resins which combines good lubricating properties and good mold release properties in one composition, thereby reducing the number of additives that need to be incorporated into the resin.
It would additionally be desirable to provide a composition which is an efficient lubricant or mold release additive thereby reducing the amount needed to be incorporated into the polymer in order to achieve the desired result. Reduction of the amount of additive employed not only is more economical but additionally results in less overall deterioration of polymer physical properties.

Finally it would be desirable to provide a lubricant which may be surface coated onto particulated thermoplastic resins to provide good solid particle lubrication (thereby achieving improved solid flow and handling properties and improved extruder feed and mixing) which properties are enhanced due to concentration of the additive as an evenly dispersed film on the surfaces of th particulated thermoplastic resin; subsequent effective incorporation into the polymeric melt for good melt lubrication; and desired mold release performance.
It is an object of this invention to overcome the above disadvantages and to provide at least some of the desirable lubricant features discussed above.
THE INVENTION
In accordance with this invention, there is provided a composition comprising a thermoplastic resin an an effective lubricating amount of a branched guerbet alcohol derived ester having the formula
CH3(CH2)

wherein R is hydrogen, -CO-alkyl or -CO-alkenyl; each R1 i independently alkyl or alkenyl; said alkyl or alkenyl radicals having from 5 to 25 carbon atoms; each R» is independently hydrogen, methyl or ethyl; m and n are each integers having a value of from 0 to 150; p is an integer having a value of from 4 to 12 and s is an integer having value of from 2 to 36.

Preferred lubricating agents of this invention- are those where each of m and n have a value of from 0 to 15; R is -CO-alkyl; R’ is alkyl containing from 6 to 20 carbon atoms; p has a value of from 4 to 8 and s has a value of from 6 to 16. Particularly preferred are those where each , R1 is alkyl having from 8 to 10 carbon atoms, m and n are zero and R is CO-C15 to C19 alkyl.
It is recognized that one technique for preparing branched guerbet alcohol derived esters involves the reaction of a guerbet alcohol or guerbet alcohol alkoxylate with a hydroxy substituted fatty acid, alkoxylate or alkoyl derivative thereof. Under the reaction conditions employed it is possible to prepare additional transesterification products, including oligomers and polymers. For example, the esterification of 12-stearoyloxy stearic acid with a guerbet alcohol may result in the preparation of an equilibrium mixture of all possible products including 2-octyldodecyl-12-stearoyloxy stearate, 2-octyldodecyl stearate, the self esterified cyclic derivative

and/or oligomeric or polymeric derivatives. These oligomeric or polymeric derivatives are the result of reaction between the hydroxyl functionality of the hydroxy substituted fatty acid and the acid functionality of a neighboring molecule under ester exchange conditions. These oligomeric or polymeric derivatives correspond to the formula:

CH3 (CH20_CH(CH2)SC-(OCHR»CH2)nOCH2CHR»
O C2H4R’
»

wherein R», R1, n, p and s are as previously defined, and is an integer from 1 to 10. Thus it is understood that th lubricants employed in the present invention need not be pure compositions having the stated formula but more often comprise mixtures of the stated products and related by-products of the reaction.
Included within the invention is a composition comprising a thermoplastic resin and an effective lubricating quantity of the reaction product which results from contacting under esterification conditions:
(1) a guerbet alcohol having the formula:
CH2CH2R’ R’CHCH20(CH2CHRO)nH
wherein R’ is C5_ 5 alkyl or alkenyl, R» is independently hydrogen, methyl or ethyl, and n is an integer having a value of from 0 to 50;
(2) a hydroxy substituted carboxylic acid havin the formula:
OfCHjCH ‘OJ-aH
CH3 (CH2)pCH(CH2)sCOOH

wherein R» is as previously defined, m is an integer having a value from 0 to 150, p is an integer having a value of from 4 to 12, and s is an integer having a value of from 2 to 36; and
(3) an aliphatic carboxylic acid corresponding to the formula:
HOR
wherein R is CO-alkyl or CO-alkenyl, said alkyl or alkenyl radicals having from 5 to 25 carbon atoms.
Preferred esterification conditions are to contact components (1) , (2) and (3) in any order at temperatures from 100°C. to 200°C. for a time sufficient to form the ester product. Water formed during the reaction may be removed by vacuum. An esterification catalyst such as an acid, metallic tin, tin compounds, organic titanates, etc. may additionally be employed if desired.
The thermoplastic resins which are benefited by inclusion of the present guerbet derived lubricants include resins of polystyrene, polyvinyl chloride, polyphenylene oxide, styrene-acrylonitrile copolymer (_»AN) , polysulfones, polyarylates, polyamides, polyimides, polyesters, butadiene rubber modified SAN (ABS) , ethylene-propylene-diene rubber modified SAN (AES) , polycarbonate, polyester carbonates and the like including mixtures and polymeric amalgams thereof; polycarbonate thermoplastic resins being preferred.
Among the various types of polycarbonates, those derived from the reaction of phosgene or the transesterification of diphenyl carbonate with diphenolic compounds of the following formula are preferred.

where Rl f R2, R3 and R4 are each independently hydrogen, lower alkyl or halogen; r has a value of 0 or l and X is -SO-;

alkylene; alkylidene; phenyl substituted alkylene or phen substituted alkylidene; cycloalkylene, monoalkyl- or polyalkyl-phenylene; cycloalkylidene, or ether, thioether, ketone, sulfone or sulfoxide containing derivatives thereof, having up to 30 carbons. Examples of these preferred thermoplastic polycarbonates include those prepared from ,4•-isopropylidene diphenol (bisphenol A),
4,4′-dihydroxydiphenyl,
1,1-bis(4-hydroxyphenyl)-1-phenylethane,
2,4-bis(4-hydroxyphenyl)-2-methyl butane,
1,1-bis(4-hydroxyphenyl)-cyclohexane
2 ,3-bis(4-hydroxyphenyl)-sulfoxide,
2 ,2-bis(3-methy1-4-hydroxyphenyl)-propane
2,4-bis(3-chloro-4-hydroxyphenyl)-butane
2,4-bis(4-hydroxyphenyl)2-butene
2,3-bis(3,5-dimethy1-4-hydroxyphenyl)-propane
2,3-bis(3,5-diethy1-4-hydroxyphenyl)-2-methylbutane
2,2-bis(3,5-dichloro-4-hydroxyphenyl)-propane
2,2-bis(3,5-dibromo-4-hydroxyphenyl)-propane. A highly preferred polycarbonate is bisphenol A polycarbonate.

Also, the aromatic polycarbonates can be branched due to the incorporation of small amounts, preferably of between 0.05 and 2.0 mol % (relative to diphenols employed) , of polyfunctional compounds, especially compounds with three or more phenolic hydroxyl groups.
Polycarbonates of this type are described, for example, in German Offenlegungsschriften (German Published Specifications) Nos. 1,570,533, 1,595,762, 2,116,974 and 2,113,347; British Patent Specification No. 1,079,821; U.S. Patent No. 3,544,514 and German Patent Application No. P 25 00 092.4.
Some examples of compounds with three or more phenolic hydroxyl groups which can be used are: phloroglucinol,
4,6-dimethyl-2,4,6-tri-4-hydroxyphenyl)-heptane-2, 4,6-dimethyl-2,4,6-tri-(4-hydroxyphenyl)-heptane, 1,4,5-tri-(4-hydroxyphenyl)-benzene, 1,1,1-tri-(4-hydroxyphenyl)-ethane, tri-(4^hydroxyphenyl)-phenylmethane,
2,2-bis-( ,4-bis-(4-hydroxyphenyl)-cyclohexyl)-propane, 2, -bis-(4-hydroxyphenylisopropyl)-phenol, 2,6-bis-(2-hydroxy-5-methylbenzyl)-4-methylphenol, 2-(4-hydroxyphenol) , 2-2,4-(dihydroxyphenyl)-propane, hexa(4-(4-hydroxyphenylisopropyl)phenyl)orthoterephthalic acid ester, tetra-(4-hydroxyphenyl)-methane and 1,4-bis-((4′ ,4″-dihydroxytriphe yl)methyl)-benzene. Other polyfunctional compounds include 2,4-dihydroxybenzoic acid and trimesic acid.
The thermoplastic polymers employed in the present compositions preferably have a mean weight average molecular weight of from about 10,000 to 3 million. Polycarbonates employed in the present compositions preferably have a mean weight-average molecular weight of

from 10,000 to 200,000; most preferably from 20,000 to 80,000; (as determined by measurement of relative viscosit in CH2C12 at 25°C. at a concentration of 0.5% by weight using a polystyrene standard) .
The thermoplastic polymer or mixture of thermoplastic polymers are mixed in particulate form with the present lubricant or the polymer or mixture of polymer can be combined as a melt with the lubricant.
The branched guerbet alcohol derived esters are preferably employed in a concentration of from 0.01% to 2% by weight, more preferably from 0.025% to 1.0%; most preferably from 0.1% to 0.25% by weight of the total thermoplastic resin compositions.
In general the additives may be added to the polymer prior to devolatilization, or at any time prior to or during any extrusion or molding operation so as to obtain uniform incorporation and dispersion thereof. In a highly preferred embodiment there is provided a particulated thermoplastic resin product comprising a surface coating of a lubricating quantity of the above branched guerbet alcohol derived esters. Such particulate polymeric products have been found to possess improved solid handling properties, most notably reduced feed times to an extruder, faster melting and feed rates to the extruder and less entrained air into the polymer melt due to smoother feed and melting properties.
The present compositions also possess improved melt flow characteristics and mold release properties. This is particularly advantageous in polycarbonate containing formulations, in that the use of higher molecular weight resins in standard molding or extrusion equipment is possible.

The thermoplastic resin containing composition is preferably molded or extruded into facia or sheets at a temperature of between 200°C. and 400°C. under a pressure of from 2,000 to 30,000 psi; preferably at a temperature of between 260°C. and 380°C. under a pressure of from 5,000 to 20,000 psi; and most preferably between 280°C. and 350°C. The molded or extruded product is then cooled to room temperature. Other thermoplastic resins can be shaped at different temperatures, depending on their glass transition temperatures. The product can be recovered as a particulated thermoplastic polymeric product comprising a surface coating of a lubricating quantity of the present guerbet derived branched ester compound.
Additional additives and modifying components of conventional design may be incorporated into the compositions of the invention if desired. For example thermal stabilizers or antioxidants such as phosphates, phosphonates or thiophosphates; ignition resistant additives including sulfur compounds, halogenated compounds, salts and polytetrafluoroethylene; fibrous reinforcing additives, including glass, boron or graphite fibers; fillers, such as mica, talc, clays, etc., rubbery impact modifiers, such as butadiene based elastomers, acrylates, saturated rubbers and polar copolymer grafted derivatives thereof may be incorporated into the present compositions without departing from the scope of the present invention.
Although lacking many of the benefits and advantages of incorporating the present guerbet derived branched ester in a composition including the thermoplastic resin, the present resins could also be sprayed on the inner surface of a mold as a mold release agent. In this capacity the ester can be employed for molds shaping larger facia where release in a matter of seconds is not required,

e.g. in forming automotive facia. In this case guerbet derived esters can be used in an unadulterated state or they can be diluted or emulsified with an inert solvent or emulsifying agent.
Having thus described the invention, reference is now had to the following examples which illustrate preferred embodiments and comparative examples but which are not to be construed as limiting to the scope of the invention as more broadly set forth above and in the appended claims.
EXAMPLE I A 995 g. sample of Lexan 181, a bisphenol A-phosgene derived polycarbonate having an average molecular weight of 60,000, was melted and 5 g. of 2-octyldodecyl-12-stearoyl stearate ester lubricant was added and thoroughly mixed at a temperature of 330°C. for 1-1/2 minutes. The resulting mixture was then passed through a twin screw extruder at a temperature of 350°C. under 18,000 psi pressure and the polycarbonate sheet was then evaluated for clarity and for the presence of lubricant migration to the surface of the product.
It was found that the resulting extruded sheet wa uniformly clear, colorless and unmarred by distortion or bubbles. The sheet was then washed with 200 ml of isopropanol. No lubricant residue was detected in the alcohol.
COMPARATIVE EXAMPLE II Example I was repeated except that a conventional ester lubricant, pentaerythritol tetrastearate, was substituted for the lubricant of Example I. The resulting extruded sheet showed areas of deformation and possessed a yellowish color. A significant amount of lubricant residu was collected when the sheet was washed with isopropanol indicating definite migration to the surface.

EXAMPLE III
When Example 1 is repeated utilizing a copolymer of 76% styrene/24% acrylonitrile in place of the polycarbonate resin to prepare injection molded articles the resulting objects are clear, colorless and have excellent mold release properties. The same result is achieved with other thermoplastics described herein when incorporating the lubricants of this invention.
EXAMPLE IV
Extruded sheets similar to that produced in Example I are obtained when 2-octyldodecyl 6-stearoyloxy laurate, 2-hexyldodecyl 12-stearoyloxy stearate, 2-decyldodecyl 12-lauroyloxy stearate, 2-hexadecylhexadecyl 12-stearoylσxy stearate, and 2-hexadecylhexadecyl 10-hexadecoyloxy hexadecanoate or any of the guerbet derived lubricants described in the following Preparations 1-32 are substituted as the lubricant in the composition containing the thermoplastic polycarbonate.

PREPARATION OF GUERBET DERIVED LUBRICANTS
The Guerbet Alcohol (Reactant Class I)
CHoCH R 1 R’CHCH20(( CH2CHR»0)nH
Description R’ n
Reactant A C16H33 0
Reactant B C16H33 1
Reactant C C16H33 3*
Reactant D C16H33 4**
Reactant E C14H29 0
Reactant F C14H29 1***
Reactant G C14H29 3*
Reactant H iAH O 4**
* 2/1 molar ratio of ethylene oxide and propylene oxide alkoxylated derivative
** 2/1/1 molar ratio of ethylene oxide/propylene oxide/ethylene oxide alkoxylated derivative
*** ethylene oxide alkoxylated derivative

The Hydroxy Carboxylic Acid (Reactant Class II)

CH3(CH2)pCH(CH2)sC-OH
Description m £ s
Reactant Y 0 5 10
Reactant W 1* 5 10
Reactant V 3** 5 10
Reactant Z 4*** 5 10
* ethoxylated derivative
** 2/1 ethylene oxide/propylene oxide alkoxylated derivative
*** 2/1/1.ethylene oxide/propylene oxide/ethylene oxide alkoxylated derivative
Fatty Acids (Reactant Class III)
Stearic Acid Laurie Acid Caprylic Acid
Preparation 1
In a suitable glass reaction vessel is added 337.9 grams of Reactant A (Class I) and 340.1 grams of Reactant Y (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of stannous oxylate (esterification catalyst) and begin to heat.. The reaction begins as the temperature reaches 140°C. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding, 322.0 grams of stearic acid is added and the reaction is continued at

140* to 200°C. , apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.
Preparation 2
In a suitable glass reaction vessel is added 401. grams of Reactant A (Class I) and 404.27 grams of Reactant Y (Class II) under good agitation and nitrogen sparge. Add 2.0 grams of a titanate esterification catalyst and begin to heat. The reaction begins as the temperature reaches 140°C. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 194.0 grams of caprylic acid is added and the reaction is continued at 140°C. to 200°C, apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.
Preparation 3
In a suitable glass reaction vessel is added 470.35 grams of Reactant Y (Class I) and 317.8 grams of Reactant C (Class II) under good agitation and nitrogen sparge. Add 2.0 grams of a suitable esterification catalyst and begin to heat. The reaction begins as the temperature reaches 140°C. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 211.9 grams of lauric acid is added and the reaction is continued at 140°C. to 200°C. , apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.

Preparation 4
In a suitable glass reaction vessel is added 455.2 grams of Reactant D (Class I) and 279.8 grams of Reactant Y (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of tin oxide (esterification catalyst) and begin to heat. The reaction begins as the temperature reaches 140°C. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 265.0 grams of stearic acid is added and the reaction is continued at 140°C. to 200°C, apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.
Preparation 5
In a suitable glass reaction vessel is added 378.2 grams of Reactant E (Class I) and 420.1 grams of Reactant Y (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of para toluene sulfonic acid (esterification catalyst) and begin to heat. The reaction begins as the temperature reaches 140βC. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 201.7 grams of caprylic acid is added and the reaction is continued at 140° to 200°C. , apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.

Preparation 6
In a suitable glass reaction vessel is added 385.8 grams of Reactant F (Class I) and 368.5 grams of Reactant Y (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of tin oxide (esterification catalyst) and begin to heat. The reaction begins as the temperature reaches 140βC. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 245.7 grams of lauric acid is added and the reaction is continued at 140°C. to 200°C, apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.
Preparation 7
In a suitable glass reaction vessel is added 440.6 grams of Reactant H (Class I) and 287.3 grams of Reactant Y (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of a suitable esterification catalyst and begin t heat. The reaction begins as the temperature reaches 140°C. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 272.0 grams of stearic acid is added and the reaction is continued at 140°C. to 200°C. , apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.

Preparation 8
In a suitable glass reaction vessel is added 508.9 grams of Reactant H (Class I) and 331.9 grams of Reactant Y (Class II) under good agitation and nitrogen sparge. The reaction begins as the temperature reaches 140°C. Continue to heat* o 200βC. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 159.3 grams of caprylic acid is added and the reaction is continued at 140°C. to 200°C, apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.
Preparation 9
In a suitable glass reaction vessel is added 321.9 grams of Reactant A (Class I) and 371.4 grams of Reactant w (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of tin oxide (esterification catalyst) and begin to heat. The reaction begins as the temperature reaches 140°C. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 306.7 grams of stearic acid is added and the reaction is continued at 140βC. to 200°C, apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.

Preparation 10
In a suitable glass reaction vessel is added 379. grams of Reactant A (Class I) and 437.6 grams of Reactant (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of metallic tin (esterification catalyst) and begin to heat. The reaction begins as the temperature reaches 140°C. Continue to heat to 200°C. and apply vacuu as the rate of distillation slows. A minimum of 97% of th theoretical water is removed before proceeding. 183.2 grams of caprylic acid is added and the reaction is continued at 140°C. to 200°C, apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.
Preparation 11
In a suitable glass reaction vessel is added 449. grams of Reactant C (Class I) and 348.1 grams of Reactant (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of a suitable esterification catalyst and begin t heat. The reaction begins as the temperature reaches 140°C. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 202.4 grams of lauric acid is added and the reaction is continue at 140βC. to 200°C. , apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.

Preparation 12
In a suitable glass reaction vessel is added 437.3 grams of Reactant D (Class I) and 308.2 grams of Reactant W (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of a suitable esterification catalyst and begin to heat. The reaction begins as the temperature reaches 140βC. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 254.5 grams of stearic acid is added and the reaction is continued at 140°C. to 200°C. , apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.
Preparation 13
In a suitable glass reaction vessel is added 356.2 grams of Reactant E (Class I) and 453.8 grams of Reactant W (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of tin oxide (esterification catalyst) and begin to heat. The reaction begins as the temperature reaches 140°C. Continue to heat to 200βC. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 190.0 grams of caprylic acid is added and the reaction is continued at 140°C. to 200°C. , apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.

Preparation 14
In a suitable glass reaction vessel is added 366. grams of Reactant F (Class I) and 401.0 grams of Reactant (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of a suitable esterification catalyst and begin t heat. The reaction begins as the temperature reaches 140βC. Continue to heat to 200βC. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 233.1 grams of lauric acid is added and the reaction is continue at 140βC. to 200βC, apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.
Preparation 15
In a suitable glass reaction vessel is added 423. grams of Reactant H (Class I) and 316.2 grams of Reactant (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of para toluene sulfonic acid (esterification catalyst) and begin to heat. The reaction begins as the temperature reaches 140βC. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 261.1 grams of stearic acid is added and the reaction is continued at 140°C. to 200°C. , apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.

Preparation 16
In a suitable glass reaction vessel is added 485.2 grams of Reactant H (Class I) and 362.9 grams of Reactant W (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of a suitable esterification catalyst and begin to heat. The reaction begins as the temperature reaches 140βC. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 152.0 grams of caprylic acid is added and the reaction is continue at 140°C. to 200βC, apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is.-fremoved, giving the desired product, and small quantities of transesterification by-products.
Preparation 17
In a suitable glass reaction vessel is added 290.0 grams έrf Reactant A (Class I) and 433.8 grams of Reactant V (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of an organic titanate (esterification catalyst) and begi to heat. The reaction begins as the temperature reaches 140°C. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 276.3 grams of stearic acid is added and the reaction is continued at 140°C. to 200°C. , apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.

Preparation 18
In a suitable glass reaction vessel is added 335 grams of Reactant A (Class I) and 502.2 grams of Reactant (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of a suitable esterification catalyst and begin heat. The reaction begins as the temperature reaches 140°C. Continue to heat to 200°C. and apply vacuum as th rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 161.1 grams of caprylic acid is added and the reaction is continued at 140°C. to 200°C, apply vacuum as the rate o distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.
Preparation 19
In a suitable glass reaction vessel is added 407 grams of Reactant C (Class I) and 409.13 grams of Reactan V (Class II) under good agitation and nitrogen sparge. A 2.0 gram of a suitable esterification catalyst and begin heat. The reaction begins as the temperature reaches 140°C. Continue to heat to 200°C. and apply vacuum as th rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 183.5 grams of lauric acid is added and the reaction is continu at 140°C. to 200°C, apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.

Preparation 20
In a suitable glass reaction vessel is added 400.7 grams of Reactant D (Class I) and 366.1 grams of Reactant V (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of tin oxide (esterification catalyst) and begin to heat. The reaction begins as the temperature reaches 140βC. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 233.2 grams of stearic acid is added and the reaction is continued at 140°C. to 200βC. , apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.
Preparation 21
In a suitable glass reaction vessel is added 294.8 grams of Reactant E (Class I) and 487.0 grams of Reactant V (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of a suitable esterification catalyst and begin to heat. The reaction begins as the temperature reaches 140βC. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 218.4 grams of lauric acid is added and the reaction is continued at 1 0βC.,to 200βC, apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.

Preparation 22
In a suitable glass reaction vessel is added 327. grams of Reactant F (Class I) and 465.0 grams of Reactant (Class II) under good agitation and nitrogen sparge. The reaction begins as the temperature reaches 140°C. Continu to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 208.4 grams of lauric acid is added and the reaction is continued at 140°C. to 200°C, apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.
Preparation 23
In a suitable glass reaction vessel is added 386. grams of Reactant H (Class I) and 375.0 grams of Reactant (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of a suitable esterification catalyst and begin t heat. The reaction begins as the temperature reaches 140°C. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 239.0 grams of stearic acid is added and the reaction is continued at 140°C. to 200°C, apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.

Preparation 24
In a suitable glass reaction vessel is added 416. grams of Reactant H (Class I) and 403.0 grams of Reactant (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of a suitable esterification catalyst and begin t heat. The reaction begins as the temperature reaches 140βC. Continue to heat to 200βC. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 181.0 grams of lauric acid is added and the reaction is continue at 140βC. to 200°C, apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.
Preparation 25
In a suitable glass reaction vessel is added 278. grams of Reactant A (Class I) and 457.0 grams of Reactant ( lass- II) under good agitation and nitrogen sparge. Add 2.0 gram of tin oxide (esterification catalyst) and begin to heat. The reaction begins as the temperature reaches 140°C. Continue to heat to 200βC. and apply vacuum as the rate of -distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 265.0 grams of stearic acid is added and the reaction is continued at 140°C. to 200°C, apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.

Preparation 26
In a suitable glass reaction vessel is added 320. grams of Reactant A (Class I) and 525.7 grams of Reactant (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of a suitable esterification catalyst and begin heat. The reaction begins as the temperature reaches 140βC. Continue to heat to 200βc. and apply vacuum as th rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 154.5 grams of caprylic acid is added and the reaction is continued at 140βC. to 200°C, apply vacuum as the rate o distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.
Preparation 27
In a suitable glass reaction vessel is added 392 grams of Reactant C (Class I) and 432.0 grams of Reactant (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of stannous oxylate (esterification catalyst) an begin to heat. The reaction begins as the temperature reaches 140βC. Continue to heat to 200°C. and apply vacu as the rate of distillation slows. A minimum of 97% of t theoretical water is removed before proceeding. 176.4 grams of lauric acid is added and the reaction is continu at 140βC. to 200°C, apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.

Preparation 28
In a suitable glass reaction vessel is added 387.0 grams of Reactant E (Class I) and 510.36 grams of Reactant Z (Class II) under good agitation and nitrogen sparge. Begin to heat. The reaction begins as the temperature reaches 140βC. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding, and small quantities of transesterification by-products.
Prepε_ration 29
In a suitable glass reaction vessel is added 281.3 grεuns of Reactant E (Class I) and 510.3 grams of Reactant Z (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of an organic titanate (esterification catalyst) and begin to heat. The reaction begins as the temperature reaches 140βC. Continue to heat to 200°C. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is- removed before proceeding, and small quantities of transesterification by-products.
Preparation 30
In a suitable glass reaction vessel is added 312.8 grεuns of Reactant F (Class I) and 488.0 grams of Reactant Z (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of a suitable esterification catalyst and begin to heat. The reaction begins as the temperature reaches 140°C. Continue to heat to 200βC. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding, and small quεtntities of transesterification by-products.

Prβpεuration 31
In a suitable glass reaction vessel is added 373. grεuns of Reactant H (Class I) and 397.0 grams of Reactant (Class II) under good agitation and nitrogen sparge. Add 2.0 grεun of tin oxide (esterification catalyst) and begin to heat. The reaction begins as the temperature reaches 140βC. Continue to heat to 200βC. and apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed before proceeding. 230.2 grams of stearic acid is added and the reaction is continued at 140βC. to 200°C, apply vacuum as the rate of distillation slows. A minimum of 97% of the theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.
Preparation 32
In a suitable glass reaction vessel is added 400. grams of Reactant H (Class I) and 426.0 grams of Reactant (Class II) under good agitation and nitrogen sparge. Add 2.0 gram of an organic titanate (esterification catalyst) and begin to heat. The reaction begins as the temperature reaches 140°C. Continue to heat to 200°C. and apply vacuu as the rate of distillation slows. A minimum of 97% of th theoretical water is removed, giving the desired product, and small quantities of transesterification by-products.
Additional examples for the preparation of guerbe derived branched esters which can be used in this inventio to provide superior mold release and uniform lubricity in thermoplastic resin compositions are effected by substituting other guerbet alcohols wherein R’ is C5 to C 5 alkyl or alkenyl and other fatty acids to prepare esters according to formula (I) wherein p has a value of 4-12, s has a value of 2 to 36 and R is hydrogen or -CO-alkyl or -CO-alkenyl in Preparations 1-32 above.

Claims (18)

WHAT IS CLAIMED IS:

1. A composition comprising a thermoplastic resin and an effective lubricating amount of a branched guerbet alcohol derived ester having the formula

CH3(CH2)pCH(CH2)SC-(OCHR»CH2)nOCH2CHR’
0 C2H4R’
wherein R is hydrogen, -CO-alkyl or -CO-alkenyl; each R’ is independently alkyl or alkenyl, said alkyl or alkenyl radicals having from 5 to 25 carbon atoms; each R» is independently hydrogen, methyl or ethyl; m and n are each integers having a value of from 0 to 150; p is an integer having a value of from 4 to 12 and s is an integer having a value of from 2 to 36.

2. The composition of Claim 1 wherein said thermoplastic resin is a polycarbonate resin.

3. The composition of Claims 1 or 2 wherein p has a value of from 4 to 8 and s has a value of from 6 to 16.

4. The composition of Claims 1, 2 or 3 wherein R is
-C-alkyl
and m and n each have a value of from 0 to 15.

5. The composition of Claims 1, 2, 3, or 4 wherein each R’ is independently Cg to C20 alkyl.

6. The composition of Claims 1, 2, 3, 4 or 5 wherein m and n are zero.

7. The composition of Claims 1-6 wherein each R’ is independently Cg to C10 alkyl and R is -CO-alkyl having from 16 to 20 carbon atoms.

8. The composition of Claims 1-7 wherein R» is hydrogen.

9. The composition of Claims 1-8 containing from about 0.025% to about 1.0% by weight of the branched ester lubricant.

10. The process of adding an effective lubricating amount of a guerbet derived branched ester of any of Claims 1-9 to a thermoplastic resin melt before molding the resulting composition at a temperature of between 200° and 400βC.

11. The process of Claim 10 wherein said thermoplastic resin is a polycarbonate resin.

12. The process of Claims 10 or 11 wherein each R’ of said branched ester is independently C6 to C10 alkyl and R of said branched ester is -CO-alkyl having fro 16 to 20 carbon atoms.

13. The process of Claims 10-12 wherein said thermoplastic polycarbonate resin is derived from

wherein Rχ, R2, R3 and R4 are each independently hydrogen, lower alkyl or halogen; r has a value of 0 or 1 and X is -SO-,
alkylene, alkylidene, phenyl substituted alkylene, phenyl substituted alkylidene, cycloalkylene, monoalkyl or polyalkyl phenylene, cycloalkylidene or ether, thioether, ketone, sulfone or sulfoxide containing derivatives there having up to 30 carbons.

14. The shaped, molded or extruded product of t process of Claim 10.

15. The shaped, molded or extruded product of t process of Claim 11.

16. A particulated thermoplastic polymeric product comprising a surface coating of a lubricating quantity of a branched guerbet alcohol derived ester havin the formula

CH3(CH2)pCH(CH2)SC-(OCHR»CH2)nOCH2CHR»
0 C2H4R’
wherein R is hydrogen, -CO-alkyl or -CO-alkenyl, each R’ i independently alkyl or alkenyl, said alkyl or alkenyl radicals having from 5 to 25 carbon atoms; each R» is independently hydrogen, methyl or ethyl; m and n are each integers having a value of from 0 to 50, p is an integer having a value of from 4 to 12 and s is an integer having value of from 2 to 36.

17. A particulated thermoplastic polymeric product according to Claim 16 wherein the ester is 2-octyldodecyl 12-stearoyloxy stearate.

18. A composition comprising a thermoplastic resin and from 0.025 to 1 wt. % of a branched guerbet alcohol derived ester having the formula

CH3(CH2)p R»CH2)nOCH2CHR•
O C2H4R’
wherein R is hydrogen, -CO-alkyl or -CO-alkenyl; each R’ i independently alkyl or alkenyl, said alkyl or alkenyl radicals having from 5 to 25 carbon atoms; each R» is independently hydrogen, methyl or ethyl; m and n are each integers having a value of from 0 to 150; p is an integer having a value of from 4 to 12 and s is an integer having value of from 2 to 36.

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Neynaber Chemie Gmbh

ADDITIVES TO MOLDING COMPOUNDS BASED ON THERMAL CONDENSATION RESINS FOR THEIR SHAPING PROCESSING

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Revlon, Inc.
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Henkel Corporation
Polyguerbet alcohol esters

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General Electric Company
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