仲丁基醚

反应条件: temp:0.00; pressure:0.00; stir:; See reaction.notes.procedure_details.

实验步骤: From the recycle, a 76% residual gas containing 95.2 grams of n-butenes (1.7 moles) and 30.4 grams of n-butene (0.52 mole) was removed per hours, was depressured to normal atmospheric pressure in the second separator and was discharged. In the second separator 140 grams (1.9 moles) of secondary butyl alcohol and 0.7-1.4 grams of di-sec. butyl ether were obtained per hour after removing the C4 -components in the form of a 77 to 89% crude alcohol still containing 10-22% water. The space-time yield of secondary butyl alcohol was 1.6 moles per liter of catalyst an hour, the selectivity being more than 99%. was removed per hours

反应条件: temp:0.00; pressure:0.00; stir:; See reaction.notes.procedure_details.

实验步骤: The procedure described in comparison Example 1 was altered so that by use of an additional dosing pump 54 kgs of the process water (total amount 204 kgs) were charged to the n-butane/n-butene mixture (feedgas and recycle gas=3,000 kgs/h) and transferred to the evaporator. Employing the same conditions as in comparison Example 1 (155° C. to 160° C., 70 bar) a temperature of 155° C. to 162° C. could be maintained in the reactor without additional heating or cooling. In the sump of a column, average amounts of 201.3 kgs (2,720 moles) of sec. butyl alcohol and 2.1 kgs (16.2 moles) of di-sec. butyl ether were obtained per hour as an approx. 99% purity crude alcohol. 101.5 kgs of n-butene and 46.4 kgs of n-butane were obtained as an approx. 59% mixture. transferred to the evaporator as in comparison Example 1 (155° C. to 160° C., 70 bar) a temperature of 155° C. to 162° C. could be maintained in the reactor without additional heating cooling