发明名称 REMOVING METHOD FOR METHANOL FROM METHYL TERT-BUTYL ETHER
摘要 A process comprises: (a) charging a mixt. of methanol and tert. butyl alcohol in molar ratios 0.5-4:1 to an etherification reaction zone contg. a bed of an etherification catalyst under reaction conditions including pressure 30-500 psia, temp. 90-140 deg C and flow rate 0.5-20 vol. feed mixt. per vol. etherification catalyst per hour to thus form a reaction prod. comprising unreacted methanol, unreacted tert. butyl alcohol, water, isobutylene, DME and methyl tert. butyl ether (MTBE); (b) charging the reaction prod. to first MTBE recovery distn. zone and sepg. it into first lower boiling fraction contg. isobutylene, DME, methanol, water and MTBE and a second heavier fraction contg. methanol, tert. butyl alcohol and water; (c) charging the first fraction to methanol solvent extn. zone and countercurrently contacting it with water in vol. ratio 1-10:1 under extraction conditions including temp. 20-60 deg C and pressure 50-500 psia to provide overhead extract contg. isobutylene, DME, water and MTBE and a raffinate contg. methanol, MTBE, isobutylene, DME and water; (d) charging the extract to second MTBE purificn. distillation zone and separating it into second lower boiling fraction contg. isobutylene, DME and water and a second heavier fraction contg. MTBE; (e) charging the second lighter fraction to decantation sepn. zone and separating it into isobutylene fraction and water fraction; (f) charging at least part of the isobutylene fraction and added methanol to an isobutylene conversion reaction zone in molar ratio 0.3-0.8:1 methanol:isobutylene and contacting with a solid resin etherification catalyst under conditions including temp. 35-100 deg C, pressure 150-250 psia and flow rate 0.5-10 vol. per vol. catalyst per hour to convert the methanol and part of the isobutylene to MTBE and form isobutylene conversion prod. contg. MTBE, unreacted isobutylene, less than 0.5 wt.% methanol, DME, tert. butyl alcohol and water; and (g) recycling the isobutylene conversion prod. to the second MTBE purificn. distillation zone.
申请公布号 JPH09104650(A) 申请公布日期 1997.04.22
申请号 JP19960206741 申请日期 1996.08.06
申请人 TEXACO DEV CORP 发明人 KAIRU RII PURESUTON
分类号 C07B61/00;C07C41/06;C07C41/09;C07C41/38;C07C41/42;C07C43/04;(IPC1-7):C07C43/04 主分类号 C07B61/00
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