Process for catalytic vapor phase oxidation
View Patent ↗The present invention provides a process for catalytic vapor phase oxidation which prevents runaway reaction or early deterioration of a catalyst, in the production of (meth)acrylic acid or the like from propylene or isobutylene by the catalytic vapor phase oxidation process using a multi-tubular reactor, which can lead to the production thereof constantly in high yield for a long period of time. Further, the present invention provides a process for catalytic vapor phase oxidation wherein raw material gas is introduced for oxidation into reaction tubes of a multi-tubular reactor which is equipped with, as arranged within the shell of the reactor, a plurality of reaction tubes having a catalyst packed therein and a plurality of baffle plates for changing the direction of the flow of a heating medium introduced into the shell, characterized in that the temperature of the catalyst packed in a reaction tube which is not connected with at least one baffle plate is measured at plural points in the direction of an axis of the reaction tube.
1. A process for catalytic vapor phase oxidation wherein raw material gas is introduced for oxidation into reaction tubes of a multi-tubular reactor which is equipped with, as arranged within the shell of the reactor, a plurality of reaction tubes having a catalyst packed therein and a plurality of baffle plates for changing the direction of the flow of a heating medium introduced into the shell, characterized in that the temperature of the catalyst packed in a reaction tube which is not connected with at least one baffle plate is measured, wherein the temperature and the flow rate of the heating medium to be introduced into the shell is controlled on the basis of the temperature of the catalyst measured.
2. The process according to claim 1 , wherein the temperature and flow rate of the heating medium to be introduced into the shell are controlled on the basis of the temperature of the catalyst measured.
3. The process according to claim 1 , wherein the temperature of the catalyst is measured at 2 to 20 points in the direction of the axis of the reaction tube.
4. The process according to claim 1 , wherein the temperature of the catalyst is measured by using a multipoint thermocouple.
5. The process according to claim 1 , wherein the direction of the flow of the raw material gas, which flows in the reaction tubes, and the direction of a macroscopic flow of the heating medium which flows in the shell, are the same directions.
6. The process according to claim 1 , wherein a plurality of catalyst layers, which have different activities, are packed in the reaction tubes.
7. The process according to claim 1 , wherein the raw material gas contains propylene, isobutylene or (meth)acrolein, as a material to be oxidized.
8. A process for catalytic vapor phase oxidation wherein raw material gas is introduced for oxidation into reaction tubes of a multi-tubular reactor which is equipped with, as arranged within the shell of the reactor, a plurality of reaction tubes having a catalyst packed therein and plurality of baffle plates for changing the direction of the flow of a heating medium introduced into the shell, characterized in that the temperature of the catalyst packed in a reaction tube which is not connected with at least one baffle plate, and the temperature of the catalyst packed in a reaction tube which is connected with all baffle plates, are measured.
9. The process according to claim 8 , wherein the temperature and flow rate of the heating medium to be introduced into the shell are controlled on the basis of the temperature of the catalyst measured.
10. The process according to claim 8 , wherein the temperature of the catalyst is measured at 2 to 20 points in the direction of the axis of the reaction tube.
11. The process according to claim 8 , wherein the temperature of the catalyst is measured by using a multipoint thermocouple.
12. The process according to claim 8 , wherein the direction of the flow of the raw material gas, which flows in the reaction tubes, and the direction of a macroscopic flow of the heating medium which flows in the shell, are the same directions.
13. The process according to claim 8 , wherein a plurality of catalyst layers, which have different activities, are packed in the reaction tubes.
14. The process according to claim 8 , wherein the raw material gas contains propylene, isobutylene or (meth)acrolein, as a material to be oxidized.