PROCESS FOR THE LONG-TERM OPERATION OF A HETEROGENEOUSLY CATALYZED PARTIAL GAS PHASE OXIDATION OF AN ORGANIC STARTING COMPOUND

Abstract

A process for the long-term operation of a heterogeneously catalyzed partial gas phase oxidation of an organic starting compound, in which the reaction gas input mixture is partially oxidized over a fixed catalyst bed which is accommodated in two successive temperature zones A, B whose temperature is changed with increasing operating time such that the initially lower temperature increases and the difference between the two temperatures decreases.

Description

Claims

1. A process for the long-term operation of a heterogeneously catalyzed partial gas phase oxidation of an organic starting compound to an organic target compound, in which a reaction gas input mixture comprising the organic starting compound and molecular oxygen is first conducted through a freshly charged fixed catalyst bed which is installed into two spatially successive temperature zones A, B whose temperatures TA and TB are such that the difference ΔTBA between the temperature TB of the temperature zone B and the temperature TA of the temperature zone A and calculated with the higher of the two temperatures as the minuend >0° C., with the proviso that the reaction gas input mixture flows through temperature zones A, B in the time sequence “first A” and “then B”, temperature zone A extending up to a conversion of the organic starting compound of CA=from 15 to 85 mol % and the conversion of the organic starting compound increasing in temperature zone B to a value CB of ≧90 mol %, and in which, with increasing operating time, in order to counteract the reduction in the quality of the fixed catalyst bed, the temperature of temperature zones A, B is then changed, wherein, with increasing operating time, the temperature of that temperature zone which initially had the lower temperature is increased and the difference ΔTBA between the temperatures of the two temperature zones is reduced, the difference being formed by the temperature of that temperature zone which initially had the higher temperature retaining its position as the minuend.

2. The process according to claim 1, wherein the partial gas phase oxidation is that of propylene to acrolein and/or acrylic acid, or that of isobutene to methacrolein and/or methacrylic acid, or that of acrolein to acrylic acid, or that of methacrolein to methacrylic acid, or that of propane to acrylic acid, or that isobutane to methacrylic acid.

3. The process according to claim 1, wherein the organic starting compound is an organic compound from the group comprising propylene, acrolein, 1-butene, 2-butene, ethane, benzene, m-xylene, p-xylene, isobutane, isobutene, tert-butanol, isobutyraldehyde, methyl ether of tert-butanol, o-xylene, naphtalene, butadiene, ethylene, propane and methacrolein.

4. The process according to claim 1, wherein the gas phase oxidation is the partial oxidation of acrolein to acrylic acid in a two-stage gas phase partial oxidation of propylene to acrylic acid.

5. The process as claimed in one of claims 1 to 4, wherein temperature zone A had the initially lower temperature.

6. The process according to claim 5, wherein the temperature of temperature zone B is reduced with increasing operating time.

7. The process according to claim 5, wherein the temperature of temperature zone B is increased with increasing operating time.

8. The process according to any of claims 1 to 7, wherein ΔTBA does not change its preceding sign within an operating time of 12 months.

9. The process according to any of claims 1 to 8, wherein the magnitude of ΔTBA does not exceed 50° C.

10. The process according to any of claims 1 to 9, wherein the difference between the maximum reaction temperature in temperature zone A, TmaxA, and the maximum reaction temperature in temperature zone B, TmaxB, formed as TmaxA−TmaxB, is ≧0° C. both at the start of the process and in long-term operation.

11. The process according to any of claims 1 to 10, which is a partial oxidation of acrolein to acrylic acid, and CA is from 40 to 85 mol %.

12. The process according to any of claims 1 to 11, which is a partial oxidation of acrolein to acrylic acid, and both the temperature of temperature zone A and of temperature zone B in long-term operation is from 230 to 340° C.

13. The process according to any of claims 1 to 12, which is a partial oxidation of acrolein to acrylic acid, and the loading of the fixed catalyst bed with acrolein is ≧90 I(STP)/I·h and ≦300 I(STP)/I·h.

14. The process according to any of claims 1 to 13, which is a partial oxidation of acrolein to acrylic acid, and the difference between the maximum reaction temperature in temperature zone A, TmaxA, and the maximum reaction temperature in temperature zone B, TmaxB, formed as TmaxA−TmaxB, is ≧0° C. and ≦15° C. both at the start of the process and in long-term operation.

15. The process according to any of claims 1 to 10, which is a partial oxidation of propylene to acrolein and CA is from 30 to 80 mol %.

16. The process according to any of claims 1 to 10 or according to claim 15, which is a partial oxidation of propylene to acrolein, and both the temperature of temperature zone A and of temperature zone B in long-term operation is from 290 to 380° C.

17. The process according to any of claims 1 to 10 or according to either of claims 15 and 16, which is a partial oxidation of propylene to acrolein, and the loading of the fixed catalyst bed with propylene is ≧120 I(STP)/I·h and ≦300 I(STP)/I·h.

18. The process according to any of claims 1 to 17, which is carried out in a multiple catalyst tube fixed bed reactor.