Fluidization promoters

Claim 2

In a process where solid particles of a selected catalyst material are maintained as a fluidized bed in a reactor and used to catalyze a selected chemical reaction whereby at least one predetermined gaseous organic compound is produced in said reactor from one or more reactants supplied to said reactor in gaseous form, the method of improving the quality of fluidization which comprises admixing and fluidizing with said particles a solid fluidization promoter of lower apparent density and smaller average particle size than said particles so that said promoter particles remain in and form a part of said stationary fluidized bed and said mass is free of stratification, said promoter being a selected material which (a) is not one of said reactants and is substantially inert with respect to said reaction and (b) does not reduce the activity of the catalyst, the ratio of the apparent density of the promoter to the apparent density of the catalyst material not exceeding about 0.6, and said promoter being present in an amount sufficient to reduce pressure fluctuations across the fluidized bed.

Claim 3

The process of claim 1 wherein the selected catalyst material comprises an iron group catalyst and has a density in the range of about 3-5.2 gm/cc, and the promoter has a density not exceeding about 1.5 gm/cc.

Claim 4

The process of claim 1 in which the selected catalyst material is fluidized by a gas stream having a velocity at least equal to the greater of the minimum bubbling velocities for (a) the selected catalyst material and (b) the promoter.

Claim 5

The process of claim 1 where the promoter is a material from the group consisting of carbon, alumina, and silica.

Claim 6

The process of claim 2 in which the selected chemical reaction is a Fischer-Tropsch reaction involving hydrogen and carbon monoxide as reactants.

Claim 7

The process of claim 2 in which the gas stream velocity is between about 2 cm/sec. and about 60 cm/sec.

Claim 8

A catalyst composition comprising solid particles of a catalyst having a first known composition characterized by the presence of a fluidization promoter which consists of solid particles of a second different composition and is substantially chemically inert with respect to said catalyst, said promoter having a lower apparent density and a smaller average particle size than the particles of said first composition, the particles of said promoter being admixed with said particles of first known composition and the ratio between the apparent particle density of the promoter and the apparent particle density of the catalyst does not exceed about 0.6, said promoter being present in an amount which is sufficient for it to have the effect of reducing pressure fluctuations across a fluidizable bed of the said catalyst composition, and said promoter having a maximum size less than that of 80 percent of the catalyst particles and an average size not exceeding about 75% of the average size of the catalyst particles.

Claim 9

A catalyst composition comprising solid particles of a catalyst having a first known composition characterized by the presence of a fluidization promoter which consists of solid particles of a second different composition and is substantially chemically inert with respect to said catalyst, said promoter having a lower apparent density and a smaller average particle size than the particles of said first composition, the particles of said promoter being admixed with said particles of first known composition and the ratio between the apparent particle density of the promoter and the apparent particle density of the catalyst does not exceed about 0.6, said promoter being present in an amount which is sufficient for it to have the effect of reducing pressure fluctuations across a fluidizable bed of the said catalyst composition, and said promoter having a maximum size less than that of 80 percent of the catalyst particles and an average size not exceeding about 75% of the average size of the catalyst particles.

Claim 10

A process for synthesizing an organic compound according to a Fischer-Tropsch synthesis reaction comprising: disposing in a reactor a mixture of an iron group Fischer-Tropsch catalyst in particle form and a fluidization promoter in particle form having a lower density and smaller average particle size than the particles of said catalyst, introducing hydrogen and carbon monoxide as reactants into said reactor and fluidizing said catalyst and promoter so as to maintain them as a fixed fluidized bed with said reactants in contact with said catalyst, maintaining said reactor at a temperature at which said reactants will react and produce at least one selected hydrocarbon product, and recovering reaction products and unreacted reactants from said reactor.

Claim 11

A process for synthesizing an organic compound according to a Fischer-Tropsch synthesis reaction comprising: disposing in a reactor a mixture of an iron group Fischer-Tropsch catalyst in particle form and a fluidization promoter in particle form having a lower density and smaller average particle size than the particles of said catalyst, introducing hydrogen and carbon monoxide as reactants into said reactor and fluidizing said catalyst and promoter so as to maintain them as a fixed fluidized bed with said reactants in contact with said catalyst, maintaining said reactor at a temperature at which said reactants will react and produce at least one selected hydrocarbon product, and recovering reaction products and unreacted reactants from said reactor.

Claim 12

A process according to claim 8 wherein said promoter is a material which is substantially inert with respect to said catalyst and said synthesis reaction.

Claim 13

A process according to claim 8 wherein said fluidization promoter is carbon.

Claim 14

A process according to claim 10 wherein at least about 80% of the particles of said carbon fluidization promoter have a particle size of between about 5 to about 10 microns and at least about 80% of the particles of said catalyst have a particle size in the range of about 10 to about 80 microns.

Claim 15

A process according to claim 10 wherein the average particle size of said promoter is about 25% of the average particle size of the catalyst.

Claim 16

A process according to claim 10 wherein said catalyst particles have an average particle size of between about 20 and 50 microns.

Claim 17

A process according to claim 10 wherein said bed consists of between about 1 and about 8 weight percent carbon particles.

Claim 18

A process according to claim 11 wherein said catalyst particles have a particle size not exceeding about 120 microns.

Claim 19

A process according to claim 11 wherein the average particle size of said carbon fluidization promoter does not exceed about 75% of the average particle size of said catalyst.

Claim 20

In a process where solid particles of a selected Fischer-Tropsch catalyst essentially comprising an iron group material are maintained as a fluidized bed in a reactor and used to catalyze a Fischer-Tropsch gas phase reaction involving hydrogen and carbon monoxide gases as reactants whereby at least one predetermined organic compound is produced in said reactor, the method of improving the quality of fluidization which comprises admixing and fluidizing with said particles of catalyst a solid fluidization promoter comprising carbon particles having an average particle size of 5-10 microns which is smaller than the average particle size of the catalyst particles so that substantially all of said carbon particles remain in and form a part of said fluidized bed and do not form a separate strata in said fluidized bed, the ratio of the apparent density of said carbon particles to the apparent density of the catalyst particles not exceeding about 0.6 and said carbon particles being present in an amount sufficient to cause pressure fluctuations across the fluidized bed to be lower than when the fluidized bed is free of said carbon particles.

Claim 21

In a process where solid particles of a selected Fischer-Tropsch catalyst essentially comprising an iron group material are maintained as a fluidized bed in a reactor and used to catalyze a Fischer-Tropsch gas phase reaction involving hydrogen and carbon monoxide gases as reactants whereby at least one predetermined organic compound is produced in said reactor, the method of improving the quality of fluidization which comprises admixing and fluidizing with said particles of catalyst a solid fluidization promoter comprising carbon particles having an average particle size of 5-10 microns which is smaller than the average particle size of the catalyst particles so that substantially all of said carbon particles remain in and form a part of said fluidized bed and do not form a separate strata in said fluidized bed, the ratio of the apparent density of said carbon particles to the apparent density of the catalyst particles not exceeding about 0.6 and said carbon particles being present in an amount sufficient to cause pressure fluctuations across the fluidized bed to be lower than when the fluidized bed is free of said carbon particles.

Claim 22

The process of claim 17 in which the fluidization promoter has an average particle size not exceeding about 75% of the average particle size of the selected catalyst material.

Claim 23

In a process where solid particles of a selected iron group Fischer-Tropsch catalyst material are maintained as a fluidized bed in a reactor and used to catalyze a selected chemical reaction whereby at least one predetermined organic compound is produced in said reactor from one or more reactants, the method of improving the quality of fluidization which comprises admixing with said particles prior to fluidization thereof a solid fluidization promoter consisting of carbon particles so that on fluidization said promoter particles are fluidized and remain in and form a part of said fluidized bed, said iron group material having an apparent density in the range of about 3 to about 5.2 gm/cc and said carbon particles having an apparent density not exceeding about 1.5 gm/cc, said iron group material also having a particle size not exceeding about 80 microns and said carbon particles having an average particle size not exceeding about 75% of the average particle size of said iron group material.

Claim 24

In a process where solid particles of a selected iron group Fischer-Tropsch catalyst material are maintained as a fluidized bed in a reactor and used to catalyze a selected chemical reaction whereby at least one predetermined organic compound is produced in said reactor from one or more reactants, the method of improving the quality of fluidization which comprises admixing with said particles prior to fluidization thereof a solid fluidization promoter consisting of carbon particles so that on fluidization said promoter particles are fluidized and remain in and form a part of said fluidized bed, said iron group material having an apparent density in the range of about 3 to about 5.2 gm/cc and said carbon particles having an apparent density not exceeding about 1.5 gm/cc, said iron group material also having a particle size not exceeding about 80 microns and said carbon particles having an average particle size not exceeding about 75% of the average particle size of said iron group material.

Claim 25

The process of claim 19 wherein said carbon particles have a particle size of between about 5 and 10 microns.

Claim 26

In a process where solid particles of alkali-promoted Fischer-Tropsch catalyst comprising an iron group material are maintained as a fluidized bed in a reactor and used to catalyze a selected gas phase chemical reaction whereby at least one predetermined organic compound is produced in said reactor from one or more gaseous reactants, the method of improving the quality of fluidization which comprises admixing and fluidizing with said particles a solid fluidization promoter of lower apparent density and smaller average particle size than said particles so that said promoter particles are fluidized and remain in and form a part of said fluidized bed, said promoter being a selected material which (a) is substantially inert with respect to said reaction and (b) does not reduce the activity of the catalyst, the ratio of the apparent density of the promoter to the apparent density of the catalyst not exceeding about 0.6, and said promoter being present in an amount sufficient to reduce pressure fluctuations across the fluidized bed.

Claim 27

In a process where solid particles of alkali-promoted Fischer-Tropsch catalyst comprising an iron group material are maintained as a fluidized bed in a reactor and used to catalyze a selected gas phase chemical reaction whereby at least one predetermined organic compound is produced in said reactor from one or more gaseous reactants, the method of improving the quality of fluidization which comprises admixing and fluidizing with said particles a solid fluidization promoter of lower apparent density and smaller average particle size than said particles so that said promoter particles are fluidized and remain in and form a part of said fluidized bed, said promoter being a selected material which (a) is substantially inert with respect to said reaction and (b) does not reduce the activity of the catalyst, the ratio of the apparent density of the promoter to the apparent density of the catalyst not exceeding about 0.6, and said promoter being present in an amount sufficient to reduce pressure fluctuations across the fluidized bed.

Claim 28

A catalyst composition comprising solid particles of an iron group catalyst for carrying out a Fischer-Tropsch synthesis reaction characterized by the presence of a fluidization promoter which consists of solid particles of carbon and is substantially chemically inert with respect to said catalyst, said carbon promoter having a lower apparent density and a smaller average particle size than the particles of said iron group catalyst, the particles of said carbon promoter being admixed with said particles of iron group catalyst composition so that said catalyst composition comprises between about 1 and about 8 weight percent carbon promoter and the ratio between the particle density of the carbon promoter and the particle density of the iron group catalyst does not exceed about 0.6, said promoter and catalyst particles being fluidizable by at least one gas from the class consisting of hydrogen and carbon monoxide so that substantially all of said promoter particles remain in admixture with said catalyst particles, said gas having a velocity through the bed at least equal to the greater of the minimum bubbling velocities for (a) the catalyst and (b) the carbon promoter.

Claim 29

A catalyst composition comprising solid particles of an iron group catalyst for carrying out a Fischer-Tropsch synthesis reaction characterized by the presence of a fluidization promoter which consists of solid particles of carbon and is substantially chemically inert with respect to said catalyst, said carbon promoter having a lower apparent density and a smaller average particle size than the particles of said iron group catalyst, the particles of said carbon promoter being admixed with said particles of iron group catalyst composition so that said catalyst composition comprises between about 1 and about 8 weight percent carbon promoter and the ratio between the particle density of the carbon promoter and the particle density of the iron group catalyst does not exceed about 0.6, said promoter and catalyst particles being fluidizable by at least one gas from the class consisting of hydrogen and carbon monoxide so that substantially all of said promoter particles remain in admixture with said catalyst particles, said gas having a velocity through the bed at least equal to the greater of the minimum bubbling velocities for (a) the catalyst and (b) the carbon promoter.

Claim 30

A catalyst composition according to claim 22 wherein said iron group catalyst has an apparent density in the range of between about 3 and about 5.2 gm/cc and a particle size not exceeding about 80 microns, and said carbon particles have an apparent density not exceeding about 1.5 gm/cc and an average particle size not exceeding about 75% of the average particle size of said iron group catalyst.

Claim 31

In a process where solid particles of a selected Fischer-Tropsch catalyst comprising an iron group material are contacted by hydrogen and carbon monoxide gases flowing at a superficial gas velocity of 20-50 cm/sec. and maintained as a fluidized bed in a reactor and used to catalyze a selected vapor phase chemical reaction whereby at least one predetermined organic compound is produced in said reactor by reaction of said hydrogen with said carbon monoxide, the method of improving the quality of fluidization which comprises admixing and fluidizing with said particles a solid fluidization promoter of lower apparent density and smaller average particle size than said particles so that said promoter particles form a part of said fluidized bed and said bed is free of classification of said catalyst and promoter, said catalyst having an apparent density in the range of about 3-5.2 gm/cc, a particle size not exceeding about 120 microns and an average particle size between about 20 and about 50 microns, said promoter being carbon and having a smaller average particle size than said catalyst with at least about 80% of the promoter particles being between about 5 and about 10 microns, said promoter being present in an amount which is sufficient to reduce pressure fluctuations across said bed.

Claim 32

In a process where solid particles of a selected Fischer-Tropsch catalyst comprising an iron group material are contacted by hydrogen and carbon monoxide gases flowing at a superficial gas velocity of 20-50 cm/sec. and maintained as a fluidized bed in a reactor and used to catalyze a selected vapor phase chemical reaction whereby at least one predetermined organic compound is produced in said reactor by reaction of said hydrogen with said carbon monoxide, the method of improving the quality of fluidization which comprises admixing and fluidizing with said particles a solid fluidization promoter of lower apparent density and smaller average particle size than said particles so that said promoter particles form a part of said fluidized bed and said bed is free of classification of said catalyst and promoter, said catalyst having an apparent density in the range of about 3-5.2 gm/cc, a particle size not exceeding about 120 microns and an average particle size between about 20 and about 50 microns, said promoter being carbon and having a smaller average particle size than said catalyst with at least about 80% of the promoter particles being between about 5 and about 10 microns, said promoter being present in an amount which is sufficient to reduce pressure fluctuations across said bed.