METHOD FOR THE MANUFACTURE OF EPOXIDES FROM 1,2-GLYCOLS

Abstract: The vapor phase dehydration of 1,2 glycols to epoxides is carried out directly, without forming an ester intermediate, over an alkali metal phosphate catalyst supported or unsupported on a carrier, preferably supported on α-alumina.

Description: METHOD FOR THE MAl4UFACTURE OF EPOXIDES FROM 1,2-GLYCOLS This invention relates to the manufacture of epoxides. More specifically, this invention relates to the manufacture of epoxides from 1,2 glycols. In one of its more specific aspects, this invention pertains to a method for converting 1,2 propylene glycol directly to propylene oxide without forming an ester intermediate. The vapor phase and liquid phase cracking of propylene glycol monoacetate ester to propylene oxide is well known. In general for this process feeds include various mixtures of propylene glycol mono- and di-acetate often containing same propylene glycol. However, an available source of ester, usually from the acetoxylation of propylene, is required or is generated in situ through for example, the use of a alkali metal acetate supported catalyst. U.S. 4,226,780 teaches the manufacture of propylene oxide from 1,2 propylene glycol using as the catalyst a weakly acetic carrier and an added basic alcohol metal salt of a low molecular weight carboxylic acid. It has now been found that the vapor phase dehydration of 1,2 glycols to epoxides can be carried out directly, without forming an ester intermediate, over an alkali metal phosphate catalyst supported or unsupported on a carrier. Moreover, epoxide yield is high and selectivity is excellent. According to this invention there is provided a method for the production of epoxides which comprises heating a 1,2 glycol in the vapor phase at a reaction temperature of from about 250 to 5000C. over a catalyst which consists essentially of an alkali metal phosphate supported or unsupported on a carrier. In a preferred embodiment, the process of this invention is employed to produce propylene oxide directly from 1,2 propylene glycol. In another embodiment, it has been found that the addition of acetic acid to the glycol feed significantly enhances epoxide selectivity without affecting catalyst activity. The alkali metal phosphate catalyst can be composed of any suitable alkali metal salt such as lithium, sodium and, preferably, potassium. Carriers found useful are S O(-alumina, zircon and a refractory metal oxide consisting of 94% by weight aC-alumina, 5% by weight CaO, and 1% CuO. The preferred carrier is < -alumina. In general for supported phosphates 5-20 weight percent of the salt on the carrier is employed. In the practice of this invention, the 1,2 glycol feed concentrations, acetic acid feed concentrations and residence tines based on catalyst void space can be varied between wide ranges. Preferably, 1,2 glycol feed concentrations will be within the ranye of 10-70 mol %. Acetic acid feed concentration, if employed, will be within the ranye of from about 0.5 to 5 mol %. And, residence times will be within the range of from about 0.5 and 2 seconds. Suitable phosphates are the mono, di and tri basic phosphates i.e MH2P04, M2HP04, H3PO4. The dibasic phosphates are preferred. The following examples further der,lonstrate catalyst preparation and the manufacture of epoxides according to this invention. EXAMPLE I The example demonstrates the preparation of a potassium phosphate catalyst and its use to produce propylene oxide from propylene glycol. About 5.0 grams of dipotassium hydroyen phosphate (K2HPO4) were dissolved in about 22 ml of water were added to about 50.0g of QL- alumina. The resulting mixture was dried, air calcined at 4250C. for about 10 hours and sieved to 8-14 mesh. A stainless steel tubular reactor (9/16" ID) was packed with 30 ml of the potassium phosphate catalyst. At 4010C. a feed stream of 38 mol % propylene glycol in nitrogen was vaporized and passed over the catalyst at a rate of 29.0 g propylene glycol per hour. The products were collected and analyzed by gas chromatography. The conversion of propylene glycol was 19% with a 70% propylene oxide and 19% propanal selectivity. The remaining products consisted primarily of acetone, allyl alcohol, l-propanol, propylene and acetol (hyroxyacetone). EXAMPLE II This example further demonstrates the use of the catalyst produced in Example I to produce propylene oxide from propylene glycol. Acetic acid was employed in the feed stream to improve propylene oxide selectivity. A stainless steel tubular reactor (9/16" ID) was packed with 30 rill of the catalyst. At 398 C. a feed stream of 35 mol % propylene glycol and 1.4 mol % acetic acid in nitrogen was vaporized and passed over the catalyst at a rate of 18.5 g propylene glycol per hour. The products were collected and analyzed by gas chromatography. The conversion of propylene glycol was 25% with a 77% propylene oxide and 10% propanal selectivity. The remaining products consisted primarily of acetone, allyl alcohol, l-propanol, propylene and acetol hyroxyacetone). It will be evident frora the foregoing that various modifications can be made to the present invention. Such, however, are considered as being within the scope of this invention.

Claims: CLAIMS 1.. A method for the production of an epoxide characterised in that it comprises heating a 1,2 glycol stream in the vapor phase at a reaction temperature of from about 250 to 5000C over a catalyst which consists essentially of an alkali metal phosphate supported or unsupported on a carrier. 2. A method as claimed in claim I characterised in that said alkali metal phosphate is potassium phosphate. 3. A method as claimed in claim 1 characterised in that said alkali metal phosphate is lithium phosphate. 4. A method as claimed in claim 1 characterised in that said alkali metal phosphate is sodium phosphate. 5. A method as claimed in any one of claims I to 4 characterised in that an effective amount of acetic acid is added to the 1,2 glycol stream to improve selectivity. 6. A method for the production of propylene oxide characterised in that it comprises heating a 1,2 propylene glycol stream in the vapor phase at a reaction temperature of from about 250 to about 5000C over a catalyst which consists essentially of an alkali metal phosphate supported or unsupported on a carrier. 7. A method as claimed in claim 6 characterised in that an effective amount of acetic acid is added to the 1,2 propylene glycol stream to improve selectively. 8. A method as claimed in claim 6 or claim 7 characterised in that the catalyst is supported on O°'alumina.

Inventors: GASTINGER, ROBERT G.
Applicants: ATLANTIC RICHFIELD COMPANY
Application year: 1984
Main classification: C07D301
IPC codes: B01J27, C07D303, C07D301, C07B61