Process for the manufacture of mixtures of formaldehyde and methanol by partial oxidation of methane

• US 4,243,613 A
• Filed: 09/25/1978
• Issued: 01/06/1981
• Est. Priority Date: 09/24/1977
• Status: Expired due to Term

• Current Assignee: Chemische Werke Huls Aktiengesellschaft
• Original Assignee: Chemische Werke Huls Aktiengesellschaft
• Inventors: Franke, Hans-Jurgen, Brockhaus, Rudolf
• Primary Examiner(s): Lone, Werren B.
• Application Number:
  US05/945,397
• Time in Patent Office: 834 Days
• Field of Search: 260/606, 260/604 R, 568/910
• US Class Current: 568/482
• CPC Class Codes: C07C 29/50 with molecular oxygen only
• CPC Class Codes: C07C 31/04 Methanol
• CPC Class Codes: C07C 45/33 of CHx-moieties
• CPC Class Codes: C07C 47/04 Formaldehyde

Abstract

A continuous process for the partial oxidation of methane to produce mixtures of formaldehyde and methanol wherein methane and an oxidizing gas are reacted in a reaction zone in the form of a flame and the resulting reaction mixture is cooled followed by separation of the resulting products, is further improved by controlling the velocity of the oxidizing gas so that it is 50 to 300 meters per second higher than the methane gas with the methane gas being introduced in a velocity of from 1 to 15 meters per second. Also, the stream of methane gas has a volume that is 3 to 100 times greater than the volume of the stream of oxidizing gas introduced into the reaction zone.

Claims

1. In a continuous process for the partial oxidation of methane to formaldehyde and methanol using oxygen or oxygen containing oxidizing gases, by allowing methane or a methane/inert gas mixture and oxidizing gas to flow together in a combustion tube under a pressure of more than 5 bars after the methane or the methane/inert gas mixture has been heated separately to 300°

to 600°

C., reacting the gas mixture resulting from the combination of said gases in a reaction zone of said combustion tube in the form of a flame by self-ignition at 300°

to 600°

C. to produce methanol and formaldehyde, cooling the reaction mixture and separating the resulting products, the improvement which comprises feeding the oxidizing gas concentrically into a stream of methane or a methane/inert gas mixture, the velocity of which, measured in the cylindrical section of the combustion tube, is 1 to 15 m. second^-1, the velocity of the oxidizing gas being 50 to 300 m. second^-1 higher than that of the methane or methane/inert gas mixture and the volume of the stream of methane gas being 3 to 100 times greater than that of the stream of oxidizing gas, said inert gas being a gas inert under the reaction conditions.

2. The process according to claim 1, wherein the velocity of the stream of oxidizing gas is 75 to 250 m. second^-1 higher than that of the stream of methane gas.

3. The process according to claim 1, wherein the methane and oxidizing gas are contacted at a pressure of from 10 to 120 bars in the reaction zone.

4. The process according to claim 1, wherein the oxidizing gas is heated separately to 300°

to 600°

C. before being combined and the temperature in the reaction zone ranges from 400°

to 600°

C.

5. The process according to claim 1, wherein the reaction mixture is cooled to a temperature of from 300°

to 450°

C.

6. The process according to claim 1, wherein a portion of the reaction mixture leaving the reaction zone is returned as a circulating gas after separating of condensable reaction products, said circulating gas being in a ratio of from 3:

1 to 95;

1 of the gases introduced into the reaction zone.

7. The process according to claim 1, wherein the inert gas consists essentially of nitrogen, carbon oxides with a ratio of CO:

CO₂ being between 1;

3 and 1;

10, or a mixture thereof.

8. The process according to claim 1, wherein the inert gas consists essentially of nitrogen.

9. The process according to claim 1, wherein a stream of methane gas and a stream of an oxidizing gas consisting essentially of oxygen or air are reacted at a pressure of from 20 to 50 bars, the volume of a methane gas being about 3 to 15 times greater than that of the air oxidizing gas or the volume of the methane gas being about 10 to 100 times greater than that of the oxygen oxidizing gas.

10. The process according to claim 1, wherein a stream of methane and nitrogen is contacted with a stream of air.