Preparation of tetrahydrofuran

• US 4,588,827 A
• Filed: 02/21/1985
• Issued: 05/13/1986
• Est. Priority Date: 02/23/1984
• Status: Expired due to Fees

• Current Assignee: BASF AG (BASF SE)
• Original Assignee: BASF AG (BASF SE)
• Inventors: Mueller, Herbert, Palm, Christof
• Primary Examiner(s): Raymond, Richard L.
• Application Number:
  US06/703,770
• Time in Patent Office: 446 Days
• Field of Search: 549/509
• US Class Current: 549/509
• CPC Class Codes: C07D 307/08 Preparation of tetrahydrofuran

Abstract

Tetrahydrofuran is prepared from a crude alkaline aqueous solution of butane-1,4-diol, as obtained by reaction of acetylene with aqueous formaldehyde and catylytic hydrogenation of the resulting but-2-yne-1,4-diol solution by a process in which the alkaline solution is first neutralized with sulfuric acid and water is then eliminated in the liquid phase at from 200° to 260° C., under superatmospheric pressure and in the presence of phosphoric acid.

Claims

1. A process for the preparation of tetrahydrofuran from an aqueous solution of butane-1,4-diol by eliminating water in the liquid phase at elevated temperatures, under superatmospheric pressure and in the presence of an acid, wherein a crude alkaline aqueous solution of butane-1,4-diol, obtained by reaction of acetylene with aqueous formaldehyde and catalytic hydrogenation of the resulting but-2-yne-1,4-diol solution, is, neutralized with sulfuric acid, and is then acidified by adding phosphoric acid and heated at from 200°

to 260°

C. under superatmospheric pressure.

2. A process as claimed in claim 1, wherein the elimination of water is carried out at from 230°

to 245°

C.

3. A process as claimed in claim 1, wherein the pH is brought to 2-3 by adding phosphoric acid.

4. A process as claimed in claim 1, wherein the liquid reaction mixture which has been heated at 200°

-260°

C. is cooled to below 100°

C. during a mean residence time of not less than 10 minutes and in the absence of a gas phase.

5. A process as claimed in claim 1, wherein the liquid reaction mixture is cooled to below 100°

C. during a mean residence time of from 15 to 30 minutes.

6. A process as claimed in claim 1 wherein the amount of sulfuric acid used for neutralizing the crude aqueous solution is not more than 20 equivalent per cent excess with reference to the equivalents of base present in the solution.

7. A process as claimed in claim 6 wherein the solution neutralized with sulfuric acid is then brought to a pH of 2-3 by adding phosphoric acid and water is eliminated in the presence of said phosphoric acid at from 230°

to 245°

C.

8. A process as claimed in claim 7 wherein the liquid reaction mixture which has been heated at 230°

to 245°

C. is cooled to below 100°

C. during a mean residence time of not less than 10 minutes.