| US 7,569,731 B2 | ||
| Process for the manufacture of methylmercaptan | ||
| Yiquan Yang, Xiamen (China); Qi Wang, Xiamen (China); Renchun Lin, Xiamen (China); Hongbin Zhang, Xiamen (China); Youzhu Yuan, Xiamen (China); Weiping Fang, Xiamen (China); Quanxing Zheng, Xiamen (China); Shenjun Dai, Xiamen (China); Xingguo Yan, Xiamen (China); Aiping Chen, Xiamen (China); Jan-Olaf Barth, Frankfurt am Main (Germany); Christoph Weckbecker, Gründau-Lieblos (Germany); Klaus Huthmacher, Gelnhausen (Germany); Hubert Redlingshöfer, Münchsteinach (Germany); and Sabine Ackermann, Hanau (Germany) | ||
| Assigned to Degussa AG, Düsseldorf (Germany) | ||
| Appl. No. 10/595,333 PCT Filed Sep. 29, 2004, PCT No. PCT/EP2004/010872 § 371(c)(1), (2), (4) Date Jan. 26, 2007, PCT Pub. No. WO2005/040082, PCT Pub. Date May 06, 2005. |
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| Claims priority of application No. 2003 1 0100495 (CN), filed on Oct. 10, 2003; application No. 2003 1 0100496 (CN), filed on Oct. 10, 2003; and application No. 2004 1 0008377 (CN), filed on Mar. 12, 2004. | ||
| Prior Publication US 2007/0213564 A1, Sep. 13, 2007 | ||
| Int. Cl. C07C 319/16 (2006.01) | ||
| U.S. Cl. 568—70 | 21 Claims |
| 1. A continuous process for the manufacture of methylmercaptan comprising contacting in a reactor an intimate mixture of carbon
oxides, sulfur or hydrogen sulfide and hydrogen as reactants in a proportion of 1/0/1/0 to 1/10/10/10 at elevated temperature
of from 300-450° C. and pressure of at least 4 bar and total gas hourly space velocity of 750-3000 h−1 over a preformed solid catalyst comprising an active component of Mo—O—K-based species, an active promoter which is a mixture
of oxides or sulfides or sulfides and oxides of an element M wherein M is selected from the group consisting of iron, cobalt,
nickel, lanthanum, cerium and manganese, and the oxides have the formula MxOy where x and y are integers from 1 to 5 and, optionally, a carrier;
wherein the catalyst K2MoO4/MxOy/carrier has a weight ratio of contents equal to 0.01-0.80/0.01-0.10/1, when the active component is expressed by K2MoO4; or the catalyst MoO3/k2O/MxOy/carrier has a weight ratio of contents equal to 0.10-0.50/0.10-0.30/0.01-0.10/1, When the active component is expressed by
MoO3 and K2O.
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