Synthesis gas and nanocarbon production method and production system

Patent metadata

Field	Value
Publication number	US-2016199807-A1
Application number	US-201615078745-A
Country	US
Kind code	A1
Filing date	Mar 23, 2016
Priority date	Mar 11, 2011
Publication date	Jul 14, 2016
Grant date	—

Abstract

A synthesis gas and nanocarbon production method has a lower hydrocarbon decomposition step for decomposing lower hydrocarbon to produce hydrogen and nanocarbon, a carbon dioxide reduction step for reacting a part of the nanocarbon produced with carbon dioxide to produce carbon monoxide, and a mixing step for mixing the hydrogen and carbon monoxide produced in a predetermined ratio, thereby nanocarbon and a synthesis gas having a desired gas ratio can be simultaneously produced easily.

First claim

1 .- 11 . (canceled)

12 . A synthesis gas and nanocarbon production system, comprising:
a lower hydrocarbon decomposition reactor, in which a lower hydrocarbon supply tube for supplying lower hydrocarbon is connected thereto, a catalyst is stored in a space communicated with the lower hydrocarbon supply tube, and the space is a reaction space where the lower hydrocarbon is directly decomposed; carbon monoxide production reactor, in which a carbon dioxide supply tube for supplying carbon dioxide is connected thereto, nanocarbon is stored in a space communicated with the carbon dioxide supply tube, and the space is a reaction space where the carbon dioxide is reduced to carbon monoxide; and a mixing equipment, which is connected to the lower hydrocarbon decomposition reactor and the carbon monoxide production reactor, and in which the hydrogen produced in the lower hydrocarbon decomposition reactor and the carbon monoxide produced in the carbon monoxide production reactor are mixed.

13 . The synthesis gas and nanocarbon production system according to claim 12 , further comprising:
a heat exchanger for cooling the hydrogen produced in the lower hydrocarbon decomposition reactor; and a waste heat supply tube for supplying heat obtained by the heat exchanger to at least one of the lower hydrocarbon decomposition reactor and the carbon monoxide production reactor.

14 . The synthesis gas and nanocarbon production system according to claim 12 ,
wherein the lower hydrocarbon decomposition reactor and the carbon monoxide production reactor have a common reaction vessel, and wherein the lower hydrocarbon decomposition reactor and the carbon monoxide production reactor have a switching part configured to switch supply of the lower hydrocarbon and supply of the carbon dioxide in the lower hydrocarbon supply tube and the carbon dioxide supply tube to selectively supply them to the reaction space.

15 . The synthesis gas and nanocarbon production system according to claim 12 , further comprising:
nanocarbon collection vessel configured to collect the nanocarbon produced in the lower hydrocarbon decomposition reactor; and a nanocarbon transfer tube for transferring the nanocarbon after being collected by the nanocarbon collection vessel to the carbon monoxide production reactor.

16 . The synthesis gas and nanocarbon production system according to claim 15 , further comprising:
a pulverization part configured to pulverize the catalyst-containing nanocarbon collected by the nanocarbon collection vessel; and a separation part, which is provided at a later step of the pulverization part, and which is configured to separate high purity nanocarbon and nanocarbon containing high concentration of the catalyst, wherein the nanocarbon transfer tube is connected to the selection part so as to transfer the selected nanocarbon containing high concentration of the catalyst.

Assignees

• Japan Steel Works Ltd
• Nat University Corp Kitami Inst Of Technology

Inventors

• Nakamura Satoru
• Tada Akio

Classifications

• Y02P20/584

  Recycling of catalysts · CPC title

• C01B2203/0827

  at least part of the fuel being a recycle stream · CPC title

• B01J23/80

  with zinc, cadmium or mercury · CPC title

• C10K3/06

  by mixing with gases · CPC title

• B01J2219/00103

  in a heat exchanger separate from the reactor · CPC title