FLOWABLE TRIETHYLENEDIAMINE

Abstract: The flowability of stored triethylenediamine is improved by admixing with a flow promoting amount of a salt, amide or ester derivative of a C₈-C₂₂ fatty acid. Especially suitable flow promoting additives for triethylenediamine are salts of stearic acid.

Description: FLOWABLE TRIETHYLENEDIAMINE TECHNICAL FIELD The invention relates to trlethylenediamlne crystal and, more partlcularly, relates to powdery triethylenediamine containing flow control additives. BACKGROUND OF THE INVENTION Triethylenedlamine (TEDA), also known as l,4-diazabicyclo(2.2.2) octane, is well known in the commercial market as a catalyst or cocatalyst in the production of polyurethane plastics, elastomers and foams. A number of methods are known in the art for preparing and isolating this compound as a product of commercially acceptable purity. The production of TEDA may employ as a starting material an alkylene polyamine, mono- or bis-hydroxyethyl ptperazlne, N-aminoethyl piperazine, or alkanolamines alone or in mixture with ethylenediamine. Typically, the TEDA is isolated from the reaction mixture as a white crystalline hygroscopic product contalning a small amount of by-product aniline compounds. The TEDA product 1s generally placed on the market for commercial users in drums of about 25 kg capacity. With improved purification the synthesized TEDA product is recovered having less than about 500 ppm by-product organic amine impurities. It was found, however, that the purified commercial powdery crystalline TEDA product of thins desired low content of organic amine impurities, when stored in commercial size drums for even short periods, particularly in a moderately warm environment, tended to develop a caking, or blocking, problem. Thins bulk aggregation of the powdery crystals is belleved the result of two factors, namely (a) sublimation and recrystallization of the TEDA molecules forming a bridge between ad3acent particles and (b) hygroscopicity which also results in agglomeration of adjacent particles. Thus the stored powdery product becomes very difficult to remove from the drum by pourlng or scooping. Japanese Patent Publication 82-203039 of Toya Soda Kogyo Co., Ltd. discloses non-solidifying triethylenedlamlne compositions comprising 0.01-2 parts by weight silica per 100 parts by weight triethylenediamine crystals. The bulk density of the silica should be less than 200 g/l. U.S. 4,345,079 discloses a scoopable triethylenediamine containing a minor amount of an additive in liquid form which is a polyethylene glycol, a glycol ester, a glycol ether or an amino alcohol. Carbowax 400 polyethylene glycol was the preferred additive. SUMMARY OF THE INVENTION According to the present invention the flowability of triethylenediamine can be improved when a flow promoting amount of certain additives are admixed with the TEDA powder. The materials which are flow improving additives according to the invention are the salt, amide or ester derivative of a C8-C22 fatty acid. TEDA compositions containing additives according to the invention remain as a flowable powder for a longer period and are much easier to render free flowing than TEDA product compositions according to the prior art. DETAILED DESCRIPTION OF THE INVENTION As flow promoting additives, the fatty acid derivatives may be admixed with te TEDA powder in any manner effective to obtain good dispersion throughout the mass. The admixing may be performed at a temperature ranging from ambient up to the melting potnt of the TEDA powder. The preferred additives are those which do not adversely affect the appearance or performance of the TEDA or blends of TEDA, such as aqueous solutions or mixtures with dipropylene glycol or dimethylethanolamine in catalyzing urethane and isocyanurate formation. A flow promoting amount of the fatty acid derivatives are mixed with the TEDA powder, such as 0.01-1 parts of the fatty acid derivative per 100 parts of TEDA. While a degree of improvement in flowability is obtained when about 0.01% of the additive is used, such lower levels have not been found to afford the desired flowability of the TEDA for sufficiently long storage periods at warmer temperatures. At greater than l part/lOD parts TEDA no additional advantage is obtained. Although the fatty acid derivatives are relatively water insoluble, this does not, however, present a problem when the TEDA 1s employed in formulations in which it is dissolved in water, for example in the production of water-blow flexible polyurethane foams, because the actual use level is so low water solubility may be achieved. Water-solubility is not required where the TEDA is used as catalyst in non-aqueous urethane formulations, isocyanate polymerization or the like provided that the additive is sufficiently soluble in the polyol or other solvent or component of the formulations with which TEDA is to be mixed. The additives according to the invention are the salt, aside or ester derivative of C8-C22 fatty acids, preferably fatty acids containing 12-18 carbon atoms. The fatty acids may be saturated in that they comprise long hydrocarbon chains containing no carbon-carbon double bonds or they may be unsaturated fatty acids containing one or more carbon-carbon multiple bonds. Among the fatty acids that are suitable for making the derivatives useful in the invention, there may be included caprylic, capric, myristic, palmitic, stearic, olelc, linoleic, and linolenic acids. The salt, amide, or ester derivatives may be formed by any of the condensation reactions well known in the art such as redacting the fatty acid with the metal hydroxide, carbonate, bicarbonate or alcoholate; reacting the appropriate amine, or alcohol with the fatty acld, fatty acid halide or fatty acid ester. Many of the suitable fatty acid derivatives are commercially available. Suitable metal salts of the fatty acids comprise as the metal eomponent a Group IA metal such as lithium, sodium, or potassium; a 6roup IIA metal such as magnesium or calcium; or a 6roup IIIA metal such as aluminium. The amide moiety of the fatty acid amide additives may be substituted or unsubstituted. The substituted amlde moiety can be monoor di-N-substituted with C -C alkyl groups such as methyl, ethyl, 2-ethyl hexyl and the like. The ester derivatives of the fatty acids would include the esters of C-Cl8 branched or unbranched alkyl alcohols, such as methyl, ethyl, isopropyl, 2-ethyl hexyl and the like, as well as the diesters of polyethylene glycols of a molecular weight in the range of about 200 to about 2000. In the following examples the flowability of TEDA was tested and rated as follows: TEDA containing the indicated amount of a flow promoting additive was mixed in a Hobart mixer at speed il (139 gyrations/min.) at the specified heating mantle temperature for the specified ttme. One pound of treated TEDA was placed in a l quart glass jar wlth a large mouth, capped tightly with a plastic cap and maintained at a selected temperature. Periodically, the Jar was uncapped and a screwdriver with a shaft of l/4" x l/4" thickness and 8* length was manually driven through the TEDA tn the jar. The flowability was rated by the magnitude of the force required to get the screwdriver through the TEDA mass as follows: Poor - The screwdriver could not get through to the bottom of the jar. The entire TEDA mass was caked and difficult to break up tnto a powder. Good - The screwdriver got through to the bottom of the jar. The TEDA mass was caked but could be broken up to a lump and then to a powder with some effort. Excellent - The screwdriver got through with very little force. The entire TEDA mass broke into free flowing powder. EXAMPLE 1 Various additives were subjected to a prescreening test to determine their suitability for improving flowability of plant produced TEDA having a content of by-product amine impurities in the range of about 100-500 ppm. The designated additives were incorporated in the respective amounts set forth in Table I with 900g of TEDA. After mixing at the indicated temperature for 0.5 hours the product mixture was stored in two jars, one kept at room temperature for 16 hours and the other at 120 F (49"C) for one week. MIXIN FLOWABILITY RUN FLOW ADDI - (g) TEDA (g) TREATMENT ( F) f? 16 hr/Rr 1 wk./120 f 1 untreated poor poor 2 Tova Soda9 very good poor 3 Carbowax 400a (9) 900 RT fair poor 4 Mi Sil 233b (0.9) 900 RT good poor S Polypropylene Glycolc (4.5) 900 AT fair fair 6 Ca-Stearate (0.9) 900 RT excellent excellent 7 Polyethylene Glycold (4.5) 900 250-300 good poor 8 Polyethylene Glycol Monomethyl Ethere (4.5) 900 250-300 good fair 9 Polyethylene Glycol good, Distearatef (4.5) 900 250-300 good very good very good 10 Na-Stearate (0.9) 900 RT excellent excellent very good, 11 Al-Stearate (0.9) 900 AT excellent excellent 12 DMADh (2.25) 900 RT very good very good very good, 13 DMAD (0.9) 900 RT good good very good/ 14 2 'Ethylhexyl Stearate (2.25) 900 RT good very good very good, IS 2-Ethylhexyl Stearate (0.9) 900 RT good fair a Polyethylene glycol (400 molecular weight) marketed by Union Carbide b A colloidal silica marketed by PPG Industries, Inc. C 4,000 molecular weight d 18,000 molecular weight e 1,900 molecular weight f 1,200 molecular weight O TEDA marketed by Toya Soda Kogyo Co., Ltd. believed to contain silica h A dimethytamide of fatty acid marketed by Buckinan Labs It can be seen from Table I that untreated TEDA powder (Run 1) demonstrated poor flowability after 16 hours at room temperature and one week at 120 F. The Toya Soda TEDA product which is believed to contain silica as a flow ald (Run 2) showed very good flowability after the 16 hour/room temperature storage but showed poor flowability after one week at 120 F. Run 4 which used a colloidal silica additive gave similar performance. Polypropylene glycol (Run 5) and polyethylene glycol (Run 7) present at a level of 4.5 grams per 900 grams TEDA showed fair and good flowability, respectively, at 16 hours/room temperature and were only rated falr and poor, respectively, at one week/120eF. The monomethyl ether of polyethylene glycol (Run 8) while rated good during the room temperature test deteriorated to a fatr rating over the longer test at higher temperature. The salts of stearic acid, namely the calcium salt (Run 6), the sodium salt (Run 10) and the aluminium salt (Run 11) were all rated very good/excellent when tested after 16 hours/room temperature and, surprisingly, were all rated excellent after a week at the elevated temperature. Thins is in contrast to the prior art additives (Runs 3-5, 7 and 8) which appeared to lose performance over the extended time period and elevated temperatures. The polyethylene glycol and 2-ethylhexyl esters of stearic acid (Runs 9 and 14) at 0.5 and 0.25 wtX were at least good when tested after 16 hours/room temperature and showed additional slight flowability improvement at the one week/120 F testing. Surprisingly, the TEDA-containing 0.1 wtX 2-ethylhexyl stearate (Run 15) showed poor results after the extended/higher temperature testing. This result seems to indicate that at least about a 0.2 wtX level of 2-ethylhexyl stearate should be used. The use of an amide derivative of a fatty acid is demonstrated in Runs 12 and 13 which employed the dimethyl amide of a fatty acid at 0.25 and 0.1 wt% levels, respectively. The flowability test results at both test conditions for Runs 12 and 13 were very good for the higher additive level and at least good for the lower content level. These runs also seem to indlcate that at least 0.2 wt% of the dimethyl amide of a fatty acid should be used as a flpw additive. EXAMPLE 2 This Example presents flowability results comparing stearate salt additives versus the polyethylene glycol and silica prior art additives. The indicated amount of additive was incorporated for 100 parts powdery TEDA crystal by mixing for 0.5 hr. at room temperature in the Hobart mixer at 139 gyrations per minute. The flow additive treated TEDA was then tested for flowability at three different conditions, namely room temperature for 16-72 hours, 120 F for 7 days and 120 F for 14 days. It can be seen from Table II that Runs 16-18 musing the prior art treated TEDA all demonstrated significant deterioration in the flowability on exposure to elevated temperatures (1200F) for extended periods (1 and 2 weeks). In marked contrast, the sodium, aluminum and calcium salts of stearic acid all showed excellent flowability under the test conditions. TABLE II MIXING FLOWABILITY RUN FLOW ADDITIVES (Dbw) TREATMENT eF RT/16-72 HRS 1200F/ 7 DAYS 1200F/14 DAYS 16 CARBOWAX 400 (1.0) RT FAIR POOR POOR 17 TOYO SODA TEDA (-) -- VERY GOOD POOR VERY POOR 18 HI SIL 233 (0.1) RT GOOD POOR 19 Na-STEARATE (0.1) RT EXCELLENT EXCELLENT EXCELLENT VERY GOOD/ VERY GOOD/ 20 Na-STEARATE (0.025) RT EXCELLENT EXCELLENT EXCELLENT 21 A1-STEARATE (0.1) RT EXCELLENT EXCELLENT 22 Ca-STEARATE (0.1) AT EXCELLENT EXCELLENT a PART BY WEIGHT PER 100 PARTS TEDA EXAMPLE 3 In this Example TEDA treated with flow additives comprising esters and amides of fatty acids were compared to the prior art flowable TEDA compositions of Runs 23 and 24. Again the indicated amount of flow additive was incorporated per 100 parts of TEDA at 139 gyrations per minute in a Hobart mixer for 30 minutes at the indicated heating mantle temperature. The flow addictive treated TEDA was then tested for flowability at room temperature/16-72 hours, 1200F/7 days and 120OF/14 days. The data in Table III show that the polyethylene glycol distearate treated TEDA (Run 25) demonstrated good flowability after room temperature storage and very good flowability after storage at 1200F for one and two weeks. Although the results were always good, if the mixture temperature is below the melting point of polyethylene glycol dlstearate, its effectiveness is diminished. The TEDA composition treated with 2-ethylhexyl stearate (Run 26) showed very good flowability at the room temperature testing but showed deteriorated flowability after storage for extended time at elevated temperatures. From this result and the data for Runs 14 and 15 in Table I, it appears that the performance of 2-ethylhexyl stearate is concentration dependent with about a 0.25 wtX level preferred. Both Runs 27 and 28 of TEDA treated with a fatty acid aside demonstrated flowability under the three test conditions vastly superior to the prior art treated TEDA compositions. TABLE III MIXING FLOWABILITY FLOW ADDITIVEa (pbw) TREATMENT eF RT/16-72 HRS 1200F/ 7 DAYS 1200F/14 DAYS !3 CARBOWAX 400 (1.0) RT FAIR POOR POOR '4 TOYO SODA TEDA (-) --- VERY GOOD POOR VERY POOR POLYETHYLENE GLYCOL GOOD VERY GOOD VERY GOOD DISTEARATE (0.5) 250-300 )t. 2-ETMYLHEXYL STEARATE (0.50) AT VERY GOOD FAIR POOR > 7 (0.50) RT VERY GOOD EXCELLENT EXCELLENT GOOD/ M3 DAD (0.25) RT VERY GOOD VERY GOOD--- a PART BY WEIGHT PER 100 PARTS TEDA b A TINT OF YELLOW STATEMENT OF INDUSTRIAL APPLICATION The invention provides for improving the flowability of stored powdery TEDA crystals by the incorporation of a flow improving amount of a derivative of a fatty acid.

Claims: CLAIMS 1. A method for improving the flowability of stored triethylene- diamine which comprises mixing with the triethylenediamine a flow improving amount of a flow promoting additive which is a salt, aside, or ester derivative of a C8-C22 fatty acld. 2. The method of Claim 1 in which the flow promoting additive is a Group IA, IIA or IIIA metal salt of a C8-C22 fatty acid. 3. The method of Claim 2 in which the salt is a sodium, calcium or aluminum salt. 4. The method of Claim 1 in which the flow promoting additive is a mono- or di-(C1-C8)alkyl-N-substituted or unsubstttuted amide of a C8-C22 fatty acid. 5. The method of Claim 4 in which the flow promoting additive is a dimethylamide derivative. 6. The method of Claim l in which the flow promottng additive is an ester of a C8-C22 fatty acid with a C1 -C18 alkyl alcohol or a dlester of such fatty acid with a polyethylene glycol. 7. The method of Claim 1 in which the fatty acid contains 12 to 18 carbon atoms. 8. The method of Claim 1 in which 0.01-1 part of fatty acid derivative is mlxed with 100 parts triethylenediamine. 9. A composition consisting essentially of triethylenedlamine admixed with a flow promoting amount of a salt, amide, or ester derivative of a C8-C22 fatty acld. 10. The composition of Claim 9 in which the flow promoting addictive is a Group IA, IIA or IIIA metal salt of a C8-C22 fatty acid. 11. The composition of Claim 10 in which the fatty acid salt is a sodium, calcium or aluminium salt. 12. The composition of Claim 9 in which the flow promoting additive is a mono- or di-(C1-C8)alkyl-N-substituted or unsubstituted amide derivative of a C8-C22 fatty acid. 13. The composition of Claim 12 in which the flow promoting addictive is a dlmethylamlde derivative. 14. The composition of Claim 9 in which the flow promottng additive is an ester of a C8-C22 fatty acid with a C1 -C18 alkyl alcohol or a ester with a polyethylene glycol. 15. The composition of Claim 9 in which the fatty acid contains 12 to 18 carbon atoms. 16. The composition of Claim 9 in which 0.01-1 part of fatty acid derivative is mixed per 100 parts trlethylenediamine, 17. The composition of Claim 10 in which the fatty acid contains 12 to 18 carbon atoms. 18. The composition of Claim 17 in which 0.01-1 part of the fatty acid derivative is mixed per 100 parts triethylenediamine. 19. The composition of Claim 18 in which the fatty acid derivative is sodium stearate. 20. The method of Claim 8 in which the fatty acid derivative is sodium stearate.

Inventors: PETRELLA, ROBERT GABRIEL, SCHWARTZ, JOEL, TAKAHASHI, AKIO
Applicants: AIR PRODUCTS AND CHEMICALS, INC.
Application year: 1986
Main classification: C07D487
IPC codes: C07D487