IP Library Granted Patent US 8,993,642
Granted Patent B2
US 8,993,642 · App. 14/008,033 · Granted Mar 31, 2015

Method for producing hydrocarbon oil, fischer-tropsch synthesis reaction device, and hydrocarbon oil production system

Inventor: Yuichi Tanaka (Tokyo, JP)
Assignees: Japan Oil, Gas and Metals National Corporation; Inpex Corporation; JX Nippon Oil & Energy Corporation; Japan Petroleum Exploration Co., Ltd.; Cosmo Oil Co., Ltd.; Nippon Steel & Sumikin Engineering Co., Ltd.
C10G3/60C10G2/342B01D37/048B01D43/00C10G2300/4006B01J8/006B01J2219/00083
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 8,993,642
App. No.
14/008,033
Granted
Mar 31, 2015
Kind
B2
Abstract

The present invention provides a process for producing a hydrocarbon oil by performing a Fischer-Tropsch synthesis reaction using a reactor for a Fischer-Tropsch synthesis including a reaction apparatus having a slurry containing catalyst particles and a gaseous phase located above the slurry to obtain a hydrocarbon oil, wherein the Fischer-Tropsch reaction is performed while controlling a temperature of the slurry so that a difference T 2 −T 1 between the average temperature T 1 of the slurry and a temperature T 2 at the liquid level of the slurry in contact with the gaseous phase is 5 to 30° C.

Claims (2)

1. A process for producing a hydrocarbon oil by performing a Fischer-Tropsch synthesis reaction using a reactor for a Fischer-Tropsch synthesis comprising a reaction apparatus having a slurry containing catalyst particles and a gaseous phase located above the slurry to obtain a hydrocarbon oil, wherein

the Fischer-Tropsch reaction is performed while controlling a temperature of the slurry so that a difference T 2 −T 1 between an average temperature T 1 of the slurry and a temperature T 2 of a liquid level of the slurry in contact with the gaseous phase is 5 to 30° C.

Assignments (2)
CORRECTIVE ASSIGNMENT TO CORRECT THE EXECUTION DATE PREVIOUSLY RECORDED AT REEL: 031706 FRAME: 0219. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded May 19, 2015
From: TANAKA, YUICHI
To: JAPAN OIL, GAS AND METALS NATIONAL CORPORATION; INPEX CORPORATION; JX NIPPON OIL & ENERGY CORPORATION; JAPAN PETROLEUM EXPLORATION CO., LTD.; COSMO OIL CO., LTD.; NIPPON STEEL & SUMIKIN ENGINEERING CO., LTD.
Reel/Frame 035727/0828 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 3, 2013
From: TANAKA, YUICHI
To: JAPAN OIL, GAS AND METALS NATIONAL CORPORATION; INPEX CORPORATION; JX NIPPON OIL & ENERGY CORPORATION; JAPAN PETROLEUM EXPLORATION CO., LTD.; COSMO OIL CO., LTD.; NIPPON STEEL & SUMIKIN ENGINEERING CO., LTD.
Reel/Frame 031706/0219 →
Priority Claims (1)
JP P2011-080611 · Mar 31, 2011 · national
Continuity (1)
Related Publication 20140088204A1 · Mar 27, 2014