Process for introducing a portion withdrawn from at least one production charge of annular coated catalysts K into a reaction tube of a tube bundle reactor
A process for introducing annular coated catalysts K into a reaction tube of a tube bundle reactor, in which adhering pairs of annular coated catalysts K formed in the preparation of the annular coated catalysts K, before the introduction thereof into the reaction tube, are removed at least partly from the annular coated catalysts K.
1. A process for introducing a portion withdrawn from at least one production charge of annular coated catalysts K into a reaction tube of a tube bundle reactor for the purpose of charging this reaction tube with a fixed catalyst bed suitable for performing a heterogeneously catalyzed partial gas phase oxidation of an organic starting compound, which comprises, before the withdrawal of the portion from the at least one production charge and/or after the withdrawal but before the introduction of the portion withdrawn into the reaction tube, removing fused adhering pairs of annular coated catalysts K formed in the preparation of the at least one production charge of annular coated catalysts K at least partly from the at least one production charge and/or from the portion withdrawn.
2. The process according to claim 1 , wherein the coated catalysts K consist of an annular shaped support body and a coating of active composition applied thereto, from 4 to 10 mm, its height from 2 to 10 mm and its wall thickness from 1 to 4 mm.
3. The process according to claim 2 , wherein the active composition comprises at least one multielement oxide.
4. The process according to claim 3 , wherein the multielement oxide is one which comprises
a) the elements Mo, Fe and Bi, or
b) the elements Mo and V, or
c) the element V and additionally P and/or Ti.
5. The process according to any of claims 1 to 4 , wherein the fused adhering pairs are removed by a process for screening with the aid of a screen.
6. A process for introducing a portion withdrawn from at least one production charge of annular coated catalysts K into a reaction tube of a tube bundle reactor for the purpose of charging this reaction tube with a fixed catalyst bed suitable for performing a heterogeneously catalyzed partial gas phase oxidation of an organic starting compound, which comprises, before the withdrawal of the portion from the at least one production charge and/or after the withdrawal but before the introduction of the portion withdrawn into the reaction tube, removing adhering pairs of annular coated catalysts K formed in the preparation of the at least one production charge of annular coated catalysts K at least partly from the at least one production charge and/or from the portion withdrawn,
wherein the adhering pairs are removed by a process for screening with the aid of a screen, and
wherein, between the external diameter E and the height H of the annular coated catalyst K, the relationship H≦0.5·E is satisfied and the screen has screen orifices O 1 within whose continuous outline a rectangle R with the side lengths L and C can be inscribed with the proviso M 1 ,
L>E≧2H>C>H,
but not with the proviso M 1 *,
L>C≧2H.
7. A process for introducing a portion withdrawn from at least one production charge of annular coated catalysts K into a reaction tube of a tube bundle reactor for the purpose of charging this reaction tube with a fixed catalyst bed suitable for performing a heterogeneously catalyzed partial gas phase oxidation of an organic starting compound, which comprises, before the withdrawal of the portion from the at least one production charge and/or after the withdrawal but before the introduction of the portion withdrawn into the reaction tube, removing adhering pairs of annular coated catalysts K formed in the preparation of the at least one production charge of annular coated catalysts K at least partly from the at least one production charge and/or from the portion withdrawn, wherein the adhering pairs are removed by a process for screening with the aid of a screen, and
wherein, between the external diameter E and the height H of the annular coated catalyst K, the relationship E≧H>0.5·E is satisfied and the screen has screen orifices O 3 within whose continuous outline a rectangle R with the side lengths L and C can be inscribed with the proviso M 3 ,
L>E<2H>C>H,
but not with the proviso M 3 *,
L≧C≧2H.
8. The process according to claim 6 , wherein the screen orifice O 1 is a rectangle with the side lengths L and C.
9. The process according to claim 7 , wherein the screen orifice O 3 is a rectangle with the side lengths L and C.
10. The process according to claim 6 , wherein the screen orifice O 1 is an elongated hole which derives from a rectangle with the side lengths L and C.
11. The process according to claim 7 , wherein the screen orifice O 3 is an elongated hole which derives from a rectangle with the side lengths L and C.
12. The process according to claim 1 , which is followed by a process for heterogeneously catalyzed partial gas phase oxidation of an organic starting compound in the reaction tube charged with the fixed catalyst bed.
13. The process according to claim 12 , wherein the heterogeneously catalyzed partial gas phase oxidation is the gas phase oxidation of acrolein to acrylic acid or the gas phase oxidation of o-xylene and/or naphthalene to phthalic anhydride.
14. A process for preparing annular coated catalysts by applying a catalytic active composition to annular shaped support bodies with the aid of a liquid binder, which comprises, after the preparation process has ended, at least partly removing fused adhering pairs of coated catalyst rings formed in the preparation.
15. A process for charging reaction tubes in a tube bundle reactor with a fixed catalyst bed, which comprises charging with annular coated catalysts which have been prepared by a preparation process according to claim 14 .
16. A process according to claim 14 , which is followed by a process comprising enveloping a portion of shaped catalyst bodies with a packing medium.
17. The process according to claim 6 , wherein proviso M 1 is
2E>L>E≧2H>C>H.
18. The process according to claim 6 , wherein proviso M 1 is
1.9E>L>E≧2H>C>H.
19. The process according to claim 6 , which satisfies the following proviso M 2 :
2E>L>E≧2H>1.75H≧C≧1.25H.
20. The process according to claim 6 , which satisfies the following proviso M 2 :
1.9E>L>E≧2H>1.75H≧C≧1.25H.
21. The process according to claim 7 , which satisfies the following proviso M 4 :
2E>L>E<2H>C>H,
but not the proviso M 4 *:
L≧C≧2H.
22. The process according to claim 7 , which satisfies the following proviso M 5 :
2H>L>E<2H>C>H,
but not the proviso M 5 *:
L≧C≧2H.
23. The process according to claim 6 , which is followed by a process for heterogeneously catalyzed partial gas phase oxidation of an organic starting compound in the reaction tube charged with the fixed catalyst bed.
24. The process according to claim 23 , wherein the heterogeneously catalyzed partial gas phase oxidation is the gas phase oxidation of acrolein to acrylic acid or the gas phase oxidation of o-xylene and/or naphthalene to phthalic anhydride.
25. The process according to claim 7 , which is followed by a process for heterogeneously catalyzed partial gas phase oxidation of an organic starting compound in the reaction tube charged with the fixed catalyst bed.
26. The process according to claim 25 , wherein the heterogeneously catalyzed partial gas phase oxidation is the gas phase oxidation of acrolein to acrylic acid or the gas phase oxidation of o-xylene and/or naphthalene to phthalic anhydride.
27. A process for preparing annular coated catalysts by applying a catalytic active composition to annular shaped support bodies with the aid of a liquid binder, which comprises, after the preparation process has ended, at least partly removing adhering pairs of coated catalyst rings formed in the preparation, wherein the adhering pairs are removed by a process for screening with the aid of a screen, and wherein, between the external diameter E and the height H of the annular coated catalyst, the relationship H≦0.5·E is satisfied and the screen has screen orifices O 1 within whose continuous outline a rectangle R with the side lengths L and C can be inscribed with the proviso M 1 ,
L>E≧2H>C>H,
but not with the proviso M 1 *,
L>C≧2H.
28. A process for charging reaction tubes in a tube bundle reactor with a fixed catalyst bed, which comprises charging with annular coated catalysts which have been prepared by a preparation process according to claim 27 .
29. A process according to claim 27 , which is followed by a process comprising enveloping a portion of shaped catalyst bodies with a packing medium.
30. A process for preparing annular coated catalysts by applying a catalytic active composition to annular shaped support bodies with the aid of a liquid binder, which comprises, after the preparation process has ended, at least partly removing adhering pairs of coated catalyst rings formed in the preparation, wherein the adhering pairs are removed by a process for screening with the aid of a screen, and wherein, between the external diameter E and the height H of the annular coated catalyst K, the relationship E≧H>0.5·E is satisfied and the screen has screen orifices O 3 within whose continuous outline a rectangle R with the side lengths L and C can be inscribed with the proviso M 3 ,
L>E<2H>C>H,
but not with the proviso M 3 *,
L≧C≧2H.
31. A process for charging reaction tubes in a tube bundle reactor with a fixed catalyst bed, which comprises charging with annular coated catalysts which have been prepared by a preparation process according to claim 30 .
32. A process according to claim 30 , which is followed by a process comprising enveloping a portion of shaped catalyst bodies with a packing medium.