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Hydrogenolysis catalyst structure, hydrogenolysis device provided with said hydrogenolysis catalyst structure, and production method of hydrogenolysis catalyst structure

A technology for hydrocracking and a manufacturing method is applied in the manufacture of a catalyst structure for hydrocracking and the field of hydrocracking devices, which can solve the problems of expensive equipment and large amount of process energy, and achieve high-efficiency hydrocracking treatment. , the effect of reducing the catalytic activity

Pending Publication Date: 2020-01-14
FURUKAWA ELECTRIC CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

As described on page 22 of Non-Patent Document 1, in the hydrocracking treatment of the upgrading process, there are the following problems: the energy consumption of the process is large, and the equipment is expensive

Method used

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  • Hydrogenolysis catalyst structure, hydrogenolysis device provided with said hydrogenolysis catalyst structure, and production method of hydrogenolysis catalyst structure
  • Hydrogenolysis catalyst structure, hydrogenolysis device provided with said hydrogenolysis catalyst structure, and production method of hydrogenolysis catalyst structure
  • Hydrogenolysis catalyst structure, hydrogenolysis device provided with said hydrogenolysis catalyst structure, and production method of hydrogenolysis catalyst structure

Examples

Experimental program
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Effect test

Embodiment 1~384

[0120] [Synthesis of precursor material (A)]

[0121] A mixed aqueous solution obtained by mixing a silica agent (tetraethoxysilane (TEOS), manufactured by Wako Pure Chemical Industries, Ltd.) and a surfactant as a templating agent was prepared, and the pH was adjusted appropriately. The hydrothermal treatment was carried out under the treatment conditions of ~350°C and 100 hours. Then, the generated precipitate was filtered, washed with water and ethanol, and fired at 600° C. in air for 24 hours to obtain precursor materials (A) of the types and pore sizes shown in Tables 1 to 8. In addition, as surfactant, the following thing was used according to the kind of precursor material (A) ("kind of precursor material (A): surfactant").

[0122] ・MCM-41: cetyltrimethylammonium bromide (CTAB) (manufactured by Wako Pure Chemical Industries, Ltd.)

[0123] · SBA-1: Pluronic P123 (manufactured by BASF Corporation)

[0124] [Production of precursor materials (B) and (C)]

[0125] Nex...

Embodiment 385~768

[0141] In Examples 385 to 768, except that the conditions in the synthesis of the precursor material (A) and the preparation of the precursor materials (B) and (C) were changed as in Tables 9 to 16, the same procedure as in Example 1 was carried out. The method yields precursor material (C). In addition, the following metal salts were used depending on the type of metal microparticles|fine-particles ("metal microparticles|metal salts") used when preparing the metal-containing aqueous solution.

[0142] Co: cobalt(II) nitrate hexahydrate (manufactured by Wako Pure Chemical Industries, Ltd.)

[0143] Ni: nickel(II) nitrate hexahydrate (manufactured by Wako Pure Chemical Industries, Ltd.)

[0144] ・Fe: iron(III) nitrate nonahydrate (manufactured by Wako Pure Chemical Industries, Ltd.)

[0145] Cu: Copper(II) nitrate trihydrate (manufactured by Wako Pure Chemical Industries, Ltd.)

[0146] [Synthesis of Catalyst Structure]

[0147] Mix the precursor material (C) obtained above...

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Abstract

The purpose of the present invention is to provide a hydrogenolysis catalyst structure which can suppress reduction in catalyst activity to achieve efficient hydrogenolysis treatment in an upgrading step of a GTL process, and a hydrogenolysis device provided with said hydrogenolysis catalyst structure. This hydrogenolysis catalyst structure is characterized by comprising a carrier with a porous structure configured from a zeolite compound, and a catalytic material in the carrier, wherein the carrier has passages that communicate with each other, and the catalytic material is at least one species selected from a group consisting of metal oxide microparticles and metal microparticles and is present in at least the passages in the carrier.

Description

technical field [0001] The present invention relates to a catalyst structure for hydrocracking, particularly a catalyst structure for hydrocracking used in an upgrading step of a GTL (Gas-to-Liquid: gas-to-liquid) process, comprising the A hydrocracking apparatus for a catalyst structure for hydrocracking and a method for producing a catalyst structure for hydrocracking. Background technique [0002] The process of producing liquid fuels from natural gas is generally referred to as the GTL process. Specifically, the GTL process is composed of a synthesis gas production process, a Fischer-Tropsch (Fischer-Tropsch) synthesis process (hereinafter referred to as "FT synthesis process"), and a reforming process. The synthesis gas production process is a process of converting natural gas into synthesis gas containing carbon monoxide and hydrogen. In addition, the FT synthesis step is a step of producing a synthetic oil containing linear hydrocarbons through a Fischer-Tropsch syn...

Claims

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Application Information

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IPC IPC(8): B01J29/035B01J29/69B01J29/78B01J35/10C07B61/00C01B37/02
CPCC07B61/00B01J29/0333B01J29/14B01J29/68B01J29/7269B01J29/46C10G47/16C10G47/18B01J35/23B01J35/40B01J35/643
Inventor 增田隆夫中坂佑太吉川琢也加藤祯宏福岛将行高桥寻子马场祐一郎关根可织
Owner FURUKAWA ELECTRIC CO LTD