Method for producing unsaturated aldehyde and/or unsaturated carboxylic acid

Patent metadata

Field	Value
Publication number	US-9580376-B2
Application number	US-201414903410-A
Country	US
Kind code	B2
Filing date	Jul 17, 2014
Priority date	Jul 18, 2013
Publication date	Feb 28, 2017
Grant date	Feb 28, 2017

Abstract

Provided is a method of subjecting an alkene to partial oxidation by using a fixed bed multitubular reactor, thereby producing an unsaturated aldehyde and/or an unsaturated carboxylic acid each corresponding to the alkene, wherein a plurality of catalyst layers formed by N division (N is N≧2) with respect to a gas flow direction of a reaction tube are provided, and when a change (° C.) of hot spot temperature per 1° C. change of reaction bath temperature in the catalyst layer is designated as Sn, at least one of the plurality of catalyst layers is regulated to Sn≦6.

First claim

The invention claimed is:

1. A method for producing an unsaturated aldehyde and/or an unsaturated carboxylic acid, which is a method for producing an unsaturated aldehyde and/or an unsaturated carboxylic acid each corresponding to an alkene by partially oxidizing the alkene using a fixed bed multitubular reactor,
wherein a plurality of catalyst layers formed by N division (N is N≧3) with respect to a gas flow direction of a reaction tube are provided, and
when a change (° C.) of hot spot temperature per 1° C. change of reaction bath temperature in the catalyst layer at the time of 300 hours elapsed after a start of the reaction and varying the reaction bath temperature is designated as Sn, at least one of the plurality of catalyst layers is regulated to Sn≦6,
in which the hot spot means a maximum value of the temperatures within the catalyst layers, and is a hot spot within the catalyst layer arranged nearest to a raw material gas inlet side or in the case where no maximum value of the temperatures is present in the catalyst layer arranged nearest to the raw material gas inlet side, a maximum value of the temperatures as a hot spot within the next or subsequent catalyst layer to the catalyst layer arranged nearest to the raw material gas inlet side, and
the reaction bath temperature for determining Sn is set within a range where an alkene conversion is 90% to 99.9%.

2. The method for producing an unsaturated aldehyde and/or an unsaturated carboxylic acid according to claim 1 ,
wherein at least one of the plurality of catalyst layers is regulated to Sn≦3.

3. The method for producing an unsaturated aldehyde and/or an unsaturated carboxylic acid according to claim 1 ,
wherein a concentration of the alkene in a raw material is 7 to 12% by volume.

4. The method for producing an unsaturated aldehyde and/or an unsaturated carboxylic acid according to claim 1 ,
wherein all of the catalyst layers contain a complex metal oxide having a formulation represented by the following formula (1):
Mo 12 Bi a Fe b Co c Ni d X e Y f Z g O h   Formula (1)

X is at least one element selected from the group consisting of magnesium (Mg), calcium (Ca), manganese (Mn), copper (Cu), zinc (Zn), cerium (Ce) and samarium (Sm); Y is at least one element selected from the group consisting of boron (B), phosphorus (P), arsenic (As), antimony (Sb) and tungsten (W); Z is at least one element selected from the group consisting of sodium (Na), potassium (K), rubidium (Rb) and cesium (Cs); a to g represent atomic ratios of the respective components; h is a numerical value determined by degrees of oxidations of the catalyst components; a=0.80 to 2.0, b=1 to 3; c=3 to 7; d=2 to 4; e=0 to 10; f=0 to 10; g=0.01 to 0.10; h is expressed by the numerical value satisfying the oxidation states of other elements; d/a is 1.9 or more and 3.2 or less; d/g is 29 or more and 69 or less; and a/g is 18 or more and 39 or less.

5. The method for producing an unsaturated aldehyde and/or an unsaturated carboxylic acid according to claim 4 , wherein b=1 to 2.5, d=2 to 3.5, and a/g is 18 or more and 35 or less.

6. A method for producing an unsaturated aldehyde and/or an unsaturated carboxylic acid, which is a method for producing an unsaturated aldehyde and/or an unsaturated carboxylic acid each corresponding to an alkene by partially oxidizing the alkene using a fixed bed multitubular reactor,
wherein a plurality of catalyst layers formed by N division (N is N=3) with respect to a gas flow direction of a reaction tube are provided, and
when a change (° C.) of hot spot temperature per 1° C. change of reaction bath temperature in the catalyst layer at the time of 300 hours elapsed after a start of the reaction and varying the reaction bath temperature is designated as Sn, at least one of the plurality of catalyst layers is regulated to Sn≦6,
in which the hot spot means a maximum value of the temperatures within the catalyst layers, and is a hot spot within the catalyst layer arranged nearest to a raw material gas inlet side or in the case where no maximum value of the temperatures is present in the catalyst layer arranged nearest to the raw material gas inlet side, a maximum value of the temperature as a hot spot within the next catalyst layer to the catalyst layer arranged nearest to the raw material gas inlet side, and
the reaction bath temperature for determining Sn is set within a range where an alkene conversion is 90% to 99.9%.

7. The method for producing an unsaturated aldehyde and/or an unsaturated carboxylic acid according to claim 6 ,
wherein at least one of the plurality of catalyst layers is regulated to Sn≦3.

8. The method for producing an unsaturated aldehyde and/or an unsaturated carboxylic acid according to claim 6 ,
wherein a concentration of the alkene in a raw material is 7 to 12% by volume.

9. The method for producing an unsaturated aldehyde and/or an unsaturated carboxylic acid according to claim 6 ,
wherein all of the catalyst layers contain a complex metal oxide having a formulation represented by the following formula (1):
Mo 12 Bi a Fe b Co c Ni d X e Y f Z g O h   Formula (1)

X is at least one element selected from the group consisting of magnesium (Mg), calcium (Ca), manganese (Mn), copper (Cu), zinc (Zn), cerium (Ce) and samarium (Sm); Y is at least one element selected from the group consisting of boron (B), phosphorus (P), arsenic (As), antimony (Sb) and tungsten (W); Z is at least one element selected from the group consisting of sodium (Na), potassium (K), rubidium (Rb) and cesium (Cs); a to g represent atomic ratios of the respective components; h is a numerical value determined by degrees of oxidations of the catalyst components; a=0.80 to 2.0, b=1 to 3; c=3 to 7; d=2 to 4; e=0 to 10; f=0 to 10; g=0.01 to 0.10; h is expressed by the numerical value satisfying the oxidation states of other elements; d/a is 1.9 or more and 3.2 or less; d/g is 29 or more and 69 or less; and a/g is 18 or more and 39 or less.

10. The method for producing an unsaturated aldehyde and/or an unsaturated carboxylic acid according to claim 9 ,
wherein b=1 to 2.5, d=2 to 3.5, and a/g is 18 or more and 35 or less.

11. A method for producing an unsaturated aldehyde and/or an unsaturated carboxylic acid, which is a method for producing an unsaturated aldehyde and/or an unsaturated carboxylic acid each corresponding to an alkene by partially oxidizing the alkene using a fixed bed multitubular reactor,
wherein a plurality of catalyst layers formed by N division (N is N=2) with respect to a gas flow direction of a reaction tube are provided, and
when a change (° C.) of hot spot temperature per 1° C. change of reaction bath temperature in the catalyst layer at the time of 300 hours elapsed after a start of the reaction and varying the reaction bath temperature is designated as Sn, at least one of the plurality of catalyst layers is regulated to Sn≦6,
in which the hot spot means a maximum value of the temperatures within the catalyst layers, and is a hot spot within the catalyst layer arranged nearest to a raw material gas inlet side, and
the reaction bath temperature for determining Sn is set within a range where an alkene conversion is 90% to 99.9%.

12. The method for producing an unsaturated aldehyde and/or an unsaturated carboxylic acid according to claim 11 ,
wherein at least one of the plurality of catalyst layers is regulated to Sn≦3.

13. The method for producing an unsaturated aldehyde and/or an unsaturated carboxylic acid according to claim 11 ,
wherein a concentration of the alkene in a raw material is 7 to 12% by volume.

14. The method for prod

Assignees

• Nippon Kayaku Kk

Inventors

• Kawamura Tomoyuki
• Kurakami Tatsuhiko
• NAKAZAWA Yuuta
• Kawaguchi Toru
• Sugiyama Motohiko

Classifications

• C07C51/16 Primary

  by oxidation (C07C51/145 takes precedence) · CPC title

• B01J37/0045

  Drying a slurry, e.g. spray drying · CPC title

• C07C45/35 Primary

  in propene or isobutene · CPC title

• B01J23/8876

  Arsenic, antimony or bismuth · CPC title

• B01J2523/00

  Constitutive chemical elements of heterogeneous catalysts · CPC title