IP Library Granted Patent US 8,927,455
Granted Patent B2
US 8,927,455 · App. 13/645,189 · Granted Jan 6, 2015

Single-step precipitation method of producing magnesia-zirconia complex carrier for catalyst for oxidative dehydrogenation of n-butane, magnesium orthovanadate catalyst supported on magnesia-zirconia complex carrier, and method of producing n-butene and 1,3-butadiene using said catalyst

Inventors: Young Jin Cho (Seosan-si, KR); Yeon Shick Yoo (Seosan-si, KR); Jin Suk Lee (Seoul, KR); Ho Sik Chang (Daejeon, KR); In Kyu Song (Seoul, KR); Ho Won Lee (Seoul, KR); Jong Kwon Lee (Daejeon, KR)
Assignee: Samsung Total Petrochemicals Co., Ltd.
B01J21/10C07C11/05B01J37/0201B01J37/036C07C5/48B01J32/00B01J23/22C07C2523/22C07C2523/02B01J37/08C07C2521/06C07C11/167Y10S502/506
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Quick Facts
Patent No.
US 8,927,455
App. No.
13/645,189
Granted
Jan 6, 2015
Kind
B2
Abstract

The present invention discloses a method of producing a magnesia-zirconia complex carrier for a catalyst for oxidative dehydrogenation of n-butane through a single-step precipitation process wherein the oxidative dehydrogenation of n-butane is to produce n-butene and 1,3-butadiene from n-butane; a method of producing a magnesium orthovanadate catalyst supported by thus prepared magnesia-zirconia complex carrier; and a method of producing n-butene and 1,3-butadiene using said catalyst.

Claims (5)

1. A method for preparing a magnesia-zirconia complex carrier for a catalyst for oxidative dehydrogenation of n-butane which comprises the following steps:

(a) preparing a magnesia-zirconia solid component by a single step gel-oxalate method, which comprises the synthesis of magnesia-zirconia by mixing an alcohol solution in which a magnesium precursor and a zirconium precursor are dissolved in an alcohol with an alcohol solution of oxalic acid in which oxalic acid is dissolved in an alcohol; and

(b) obtaining a magnesia-zirconia carrier for a catalyst for oxidative dehydrogenation of n-butane by separating, drying and heating the magnesia-zirconia solid component obtained from the above step (a).

2. The method according to claim 1 , wherein, in the above step (b), drying is carried out at 50-200° C. for 3-24 hours, and heating is carried out at 350-800° C. for 1-12 hours.

3. The method according to claim 1 , wherein the alcohol is at least one selected from the group consisting of ethanol, propanol, butanol and 2-butanol.

Assignments (4)
CORRECTIVE ASSIGNMENT TO CORRECT THE RECEIVING PARTY ADDRESS PREVIOUSLY RECORDED AT REEL: 036548 FRAME: 0271. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Nov 9, 2015
From: SAMSUNG ATOFINA CO., LTD.; SAMSUNG TOTAL PETROCHEMICALS CO., LTD.
To: HANWHA TOTAL PETROCHEMICAL CO., LTD.
Reel/Frame 037071/0433 →
CHANGE OF NAME Recorded Sep 3, 2015
From: SAMSUNG ATOFINA CO., LTD.; SAMSUNG TOTAL PETROCHEMICALS CO., LTD.
To: HANWHA TOTAL PETROCHEMICAL CO., LTD.
Reel/Frame 036548/0271 →
CHANGE OF ADDRESS OF ASSIGNEE Recorded Jul 14, 2014
From: SAMSUNG TOTAL PETROCHEMICALS CO., LTD.
To: SAMSUNG TOTAL PETROCHEMICALS CO., LTD.
Reel/Frame 033312/0388 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 4, 2013
From: CHO, YOUNG JIN; YOO, YEON SHICK; LEE, JIN SUK; CHANG, HO SIK; SONG, IN KYU; LEE, HO WON; LEE, JONG KWON
To: SAMSUNG TOTAL PETROCHEMICALS CO., LTD.
Reel/Frame 029567/0372 →
Priority Claims (1)
KR 10-2011-0101954 · Oct 6, 2011 · national
Continuity (1)
Related Publication 20130090509A1 · Apr 11, 2013