The present invention relates to a catalyst for oxygen-free direct conversion of methane and a method of converting methane using the same, and more particularly to a catalyst for oxygen-free direct conversion of methane, in which the properties of the catalyst are optimized by adjusting the free space between catalyst particles packed in a reactor, thereby maximizing the catalytic reaction rate without precise control of reaction conditions for oxygen-free direct conversion of methane, minimizing coke formation and exhibiting stable catalytic performance even upon long-term operation, and to a method of converting methane using the same.

The present invention relates to a catalyst for oxygen-free direct conversion of methane and a method of converting methane using the same, and more particularly to a catalyst for oxygen-free direct conversion of methane, in which the properties of the catalyst are optimized by adjusting the free space between catalyst particles packed in a reactor, thereby maximizing the catalytic reaction rate without precise control of reaction conditions for oxygen-free direct conversion of methane, minimizing coke formation and exhibiting stable catalytic performance even upon long-term operation, and to a method of converting methane using the same.

A porous formed body (Y) including a porous formed body (X) that satisfies the following (x-1) to (x-3), and an alkali metal carbonate or an alkali metal bicarbonate, in which a content of the alkali metal carbonate or the alkali metal bicarbonate is in a range of from 1 part by mass to 230 parts by mass, with respect to 100 parts by mass of the porous formed body (X), and a production method thereof, an -olefin dimerization catalyst and a production method thereof, and a method of producing an -olefin dimer:

requirement (x-1): a volume of pores with a pore diameter in a range of from 0.01 m to 100 m is from 0.10 mL/g to 1.00 mL/g;

requirement (x-2): a median pore diameter of pores with a pore diameter in a range of from 0.01 m to 100 m is from more than 0.01 m to 10.0 m; and

requirement (x-3): a crushing strength is from 0.7 kgf to 15.0 kgf.

A porous formed body (Y) including a porous formed body (X) that satisfies the following (x-1) to (x-3), and an alkali metal carbonate or an alkali metal bicarbonate, in which a content of the alkali metal carbonate or the alkali metal bicarbonate is in a range of from 1 part by mass to 230 parts by mass, with respect to 100 parts by mass of the porous formed body (X), and a production method thereof, an -olefin dimerization catalyst and a production method thereof, and a method of producing an -olefin dimer:

requirement (x-1): a volume of pores with a pore diameter in a range of from 0.01 m to 100 m is from 0.10 mL/g to 1.00 mL/g;

requirement (x-2): a median pore diameter of pores with a pore diameter in a range of from 0.01 m to 100 m is from more than 0.01 m to 10.0 m; and

requirement (x-3): a crushing strength is from 0.7 kgf to 15.0 kgf.

The invention relates to a process for producing an oligomerization catalyst comprising nickel oxide and a silicon-alumina support material, wherein the silica-alumina support material is in the ammonium form. The present invention further relates to a process for oligomerization of C3- to C6-olefins using the oligomerization catalyst produced according to the invention.

The invention relates to a process for producing an oligomerization catalyst comprising nickel oxide and a silicon-alumina support material, wherein the silica-alumina support material is in the ammonium form. The present invention further relates to a process for oligomerization of C3- to C6-olefins using the oligomerization catalyst produced according to the invention.

Reaction device which makes possible the oligomerization of olefins to give linear olefins and preferably linear -olefins, comprising a gas/liquid reactor and a reactor of plug-flow type. The reaction device is also employed in an oligomerization process.

Reaction device which makes possible the oligomerization of olefins to give linear olefins and preferably linear -olefins, comprising a gas/liquid reactor and a reactor of plug-flow type. The reaction device is also employed in an oligomerization process.

The present invention relates to a method of preparing -olefins by oligomerization of C.sub.2-C.sub.4 olefins. The method is carried out by oligomerization of C.sub.2-C.sub.4 olefins in the presence of a catalyst system comprising a transition metal source, an activator, which is an alkylaluminoxane, and a compound of formula (I), Ar.sup.1Ar.sup.2PN(R)PAr.sup.3Ar.sup.4 [formula I], wherein Ar.sup.1-4 are the same or different and are selected from substituted or unsubstituted C.sub.6-C.sub.10 aryl, R is selected from linear or branched C.sub.1-C.sub.4 alkyl, substituted or unsubstituted C.sub.6-C.sub.10 aryl, and substituted or unsubstituted C.sub.3-C.sub.10 cycloalkyl, wherein the oligomerization is carried out in a solvent, which is a bicyclic compound or a mixture of bicyclic compounds, preferably decalin. The claimed method provides a significant increase in the activity of the catalyst during the oligomerization process and, as a consequence, a reduction in the catalyst unit consumption, as well a reduction in the formation of polymer by-product.

The present invention relates to a method of preparing -olefins by oligomerization of C.sub.2-C.sub.4 olefins. The method is carried out by oligomerization of C.sub.2-C.sub.4 olefins in the presence of a catalyst system comprising a transition metal source, an activator, which is an alkylaluminoxane, and a compound of formula (I), Ar.sup.1Ar.sup.2PN(R)PAr.sup.3Ar.sup.4 [formula I], wherein Ar.sup.1-4 are the same or different and are selected from substituted or unsubstituted C.sub.6-C.sub.10 aryl, R is selected from linear or branched C.sub.1-C.sub.4 alkyl, substituted or unsubstituted C.sub.6-C.sub.10 aryl, and substituted or unsubstituted C.sub.3-C.sub.10 cycloalkyl, wherein the oligomerization is carried out in a solvent, which is a bicyclic compound or a mixture of bicyclic compounds, preferably decalin. The claimed method provides a significant increase in the activity of the catalyst during the oligomerization process and, as a consequence, a reduction in the catalyst unit consumption, as well a reduction in the formation of polymer by-product.