Process for producing diacetoxybutanes and butanediols

Claim 2

In a process for producing a diacetoxybutane by hydrogenating a diacetoxybutene compound in the presence of a supported hydrogenation catalyst, the improvement which comprises, introducing said compound and hydrogen into a first reaction zone having said hydrogenation catalyst in a fixed bed therein, hydrogenating said compound under adiabatic conditions at a first temperature of 50° to 150° C to form a first reaction product, dividing said reaction product into a first portion and a second portion, cooling said first portion, recirculating said first portion to said first zone to maintain said first temperature, introducing said second portion and hydrogen into a second reaction zone having said hydrogenation catalyst in a fixed bed therein, further hydrogenating said second portion at a second temperature higher than said first temperature and up to 200° C.

Claim 3

A process for producing a diacetoxybutane according to claim 1, in which the reaction temperature and the reaction pressure in the first zone are 60° to 130° C and atmospheric to 100 atm. and the reaction temperature and the reaction pressure in the second zone are 80° to 170° C and atmospheric to 100 atm.

Claim 4

A process for producing a diacetoxybutane according to claim 1, in which the proportion of said divided two portions is 0.5 to 20 parts to be recirculated to the first zone per one part to be supplied to the second zone, and the portion to be recirculated is maintained at a temperature of 5° to 90° C lower than that at the outlet of the first zone.

Claim 5

A process for producing a diacetoxybutane according to claim 1, in which said supported catalyst is metallic palladium supported on active carbon having a specific surface area of from 700 to 1200 m 2 /g, said compound, said first reaction product and hydrogen being supplied to the tops of the first and second zones downwardly and concurrently.

Claim 6

A process for producing a diacetoxybutane according to claim 1, in which said diacetoxybutene is 1,4-diacetoxybutene-2.

Claim 7

A process for producing a diacetoxybutane according to claim 1, in which said hydrogen contains carbon monoxide and carbon dioxide in a proportion of less than 5 ppm.

Claim 8

In a process for producing a butanediol by hydrogenating a diacetoxybutene compound in the presence of a supported hydrogenation catalyst and effecting hydrolysis of the diacetoxybutane obtained, the improvement which comprises introducing said compound and hydrogen into a first reaction zone having said hydrogenation catalyst in a fixed bed therein, hydrogenating said compound under adiabatic conditions at a first temperature of 50° to 150° C to form a first reaction product, dividing said reaction product into a first portion and a second portion, cooling said first portion, recirculating said first portion to said first zone to maintain said first temperature, introducing said second portion and hydrogen into a second reaction zone having said hydrogenation catalyst in a fixed bed therein, further hydrogenating said second portion at a second temperature higher than said first temperature and up to 200° C, thereby producing diacetoxybutane and effecting hydrolysis of said diacetoxybutane in the presence of a solid, acid catalyst.

Claim 9

In a process for producing a butanediol by hydrogenating a diacetoxybutene compound in the presence of a supported hydrogenation catalyst and effecting hydrolysis of the diacetoxybutane obtained, the improvement which comprises introducing said compound and hydrogen into a first reaction zone having said hydrogenation catalyst in a fixed bed therein, hydrogenating said compound under adiabatic conditions at a first temperature of 50° to 150° C to form a first reaction product, dividing said reaction product into a first portion and a second portion, cooling said first portion, recirculating said first portion to said first zone to maintain said first temperature, introducing said second portion and hydrogen into a second reaction zone having said hydrogenation catalyst in a fixed bed therein, further hydrogenating said second portion at a second temperature higher than said first temperature and up to 200° C, thereby producing diacetoxybutane and effecting hydrolysis of said diacetoxybutane in the presence of a solid, acid catalyst.

Claim 10

A process for producing a butanediol according to claim 7, in which said solid acid catalyst is a sulfonic acid type cation exchange resin and said hydrolysis is effected at a temperature of from 30° to 120° C.

Claim 11

In a process for producing a butanediol by hydrogenating a diacetoxybutene compound in the presence of a supported hydrogenation catalyst and effecting hydrolysis of the diacetoxybutane obtained, the improvement which comprises introducing said compound and hydrogen into a first reaction zone having said hydrogenation catalyst in a fixed bed therein, hydrogenating said compound under adiabatic conditions at a first temperature of 60° to 130° C and under a pressure of 1 to 100 atmospheres to form a first reaction product, dividing said first reaction product into a first portion and a second portion, there being from 0.5 to 20 parts of said first portion to 1 part of said second portion, cooling said first portion to a temperature of 5° to 90° C lower than said first temperature, recirculating said first portion to said first zone to maintain said first temperature, introducing said second portion and hydrogen into a second reaction zone having said hydrogenation catalyst in a fixed bed therein, further hydrogenating said second portion at a second temperature higher than said first temperature and from 80° to 170° C and under a pressure of 1 to 100 atmospheres to produce diacetoxybutane, hydrolyzing said diacetoxybutane in the presence of a solid, acid cation exchange resin at a hydrolyzing temperature of 40° to 100° C to produce a butanediol reaction product, distilling said butanediol product to remove water and acetic acid followed by removal of unreacted and partially hydrolyzed material, and rectifying the butanediol product at a reflux ratio of up to 10 in a rectifier having up to 90 theoretical plates, whereby butanediol is recovered as an overhead.

Claim 12

In a process for producing a butanediol by hydrogenating a diacetoxybutene compound in the presence of a supported hydrogenation catalyst and effecting hydrolysis of the diacetoxybutane obtained, the improvement which comprises introducing said compound and hydrogen into a first reaction zone having said hydrogenation catalyst in a fixed bed therein, hydrogenating said compound under adiabatic conditions at a first temperature of 60° to 130° C and under a pressure of 1 to 100 atmospheres to form a first reaction product, dividing said first reaction product into a first portion and a second portion, there being from 0.5 to 20 parts of said first portion to 1 part of said second portion, cooling said first portion to a temperature of 5° to 90° C lower than said first temperature, recirculating said first portion to said first zone to maintain said first temperature, introducing said second portion and hydrogen into a second reaction zone having said hydrogenation catalyst in a fixed bed therein, further hydrogenating said second portion at a second temperature higher than said first temperature and from 80° to 170° C and under a pressure of 1 to 100 atmospheres to produce diacetoxybutane, hydrolyzing said diacetoxybutane in the presence of a solid, acid cation exchange resin at a hydrolyzing temperature of 40° to 100° C to produce a butanediol reaction product, distilling said butanediol product to remove water and acetic acid followed by removal of unreacted and partially hydrolyzed material, and rectifying the butanediol product at a reflux ratio of up to 10 in a rectifier having up to 90 theoretical plates, whereby butanediol is recovered as an overhead.