IP Library Granted Patent US 8,674,156
Granted Patent B2
US 8,674,156 · App. 12/746,558 · Granted Mar 18, 2014

Mixed manganese ferrite catalysts, method of preparing thereof and method of preparing 1,3-butadiene using thereof

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Quick Facts
Patent No.
US 8,674,156
App. No.
12/746,558
Granted
Mar 18, 2014
Kind
B2
Abstract

A method of producing a mixed manganese ferrite catalyst, and a method of preparing 1,3-butadiene using the mixed manganese ferrite catalyst. Specifically, a method of producing a mixed manganese ferrite catalyst through a coprecipitation method which is performed at a temperature of 10˜40° C., and a method of preparing 1,3-butadiene using the mixed manganese ferrite catalyst through an oxidative dehydrogenation reaction, in which a C4 mixture containing n-butene, n-butane and other impurities is directly used as reactants without performing additional n-butane separation process or n-butene extraction. 1,3-butadiene can be prepared directly using a C4 mixture including n-butane at a high concentration as a reactant through an oxidative hydrogenation reaction without performing an additional n-butane separation process, and 1,3-butadiene, having high activity, can be also obtained in high yield for a long period of time.

Claims (21)

1. A method of producing a mixed manganese ferrite catalyst for preparing 1,3-butadiene, comprising:

(A) providing an aqueous precursor solution including a manganese precursor and an iron precursor, in which atom ratio of iron (Fe) to manganese (Mn) is 1.8˜2.4;

(B) mixing the aqueous precursor solution with an alkaline solution having a molar concentration of 1.5˜4.0 M at a temperature of 10˜40° C. to form a coprecipitated solution;

(C) washing and filtering the coprecipitated solution to obtain a solid catalyst;

(D) drying the solid catalyst at 70˜200° C.; and

(E) heat-treating the dried solid catalyst at 350˜800° C. to obtain the mixed manganese ferrite catalyst consisting of iron oxide (α-Fe 2 O 3 ), manganese iron oxide (MnFeO 3 ) and manganese ferrite (MnFe 2 O 4 ).

2. The method of producing a mixed manganese ferrite catalyst according to claim 1 ,

wherein the step (B) further comprises:

stirring the aqueous precursor solution and alkaline solution for 6˜12 hours such that coprecipitation is conducted.

3. The method of producing a mixed manganese ferrite catalyst according to claim 1 , wherein the manganese precursor includes manganese chlorides or manganese nitrates, and the iron precursor includes iron chlorides or iron nitrates.

4. The method of producing a mixed manganese ferrite catalyst according to claim 3 , wherein the iron precursor is selected from the group consisting of ferrous chloride tetrahydrate, ferrous chloride hexahydrate, ferrous chloride dihydrate, ferric chloride hexahydrate, ferrous nitrate hexahydrate, ferrous nitrate nonahydrate, ferric nitrate hexahydrate and ferric nitrate nonahydrate, and the manganese precursor is selected from the group consisting of manganous chloride, manganous chloride tetrahydrate, manganic chloride, manganese tetrachloride, manganese nitrate hexahydrate, manganese nitrate tetrahydrate and manganese nitrate monohydrate.

5. The method of producing a mixed manganese ferrite catalyst according to claim 1 , wherein the step (B) is conducted at a temperature of 15˜25° C.

6. The method of producing a mixed manganese ferrite catalyst according to claim 1 , wherein the alkaline solution is a sodium hydroxide solution.

7. A mixed manganese ferrite catalyst produced using the method of claim 1 , the catalyst having peaks in 2-theta ranges of 18.78˜18.82, 24.18˜24.22, 33.2˜33.24, 35.64˜35.68, 40.9˜40.94, 45.22˜45.26, 49.56˜49.6, 54.22˜54.26, 55.24˜55.28, 57.92˜57.96, 62.56˜62.6, 64.04˜64.08, 66.02˜66.06, 72.16˜72.2 and 75.78˜75.82 in X-ray diffraction analysis.

8. A method of preparing 1,3-butadiene using a mixed manganese ferrite catalyst, comprising:

(A) providing a mixed gas of a C4 mixture, air and steam as a reactant;

(B) continuously passing the reactant through a catalyst layer supported with the catalyst produced using the method of claim 1 to conduct an oxidative dehydrogenation reaction, wherein said catalyst is the mixed manganese ferrite catalyst consisting of iron oxide (α-Fe 2 O 3 ), manganese iron oxide (MnFeO 3 ) and manganese ferrite (MnFe 2 O 4 ); and

(C) obtaining 1,3-butadiene from the catalyst layer.

9. The method of preparing 1,3-butadiene according to claim 8 , wherein the C4 mixture comprises 0.5˜50 wt % of n-butane, 40˜99 wt % of n-butene, and 0.5˜10 wt % of a balance of other constituents thereof.

10. The method of preparing 1,3-butadiene according to claim 8 , wherein, in (A), a mixing molar ratio of n-butene:air:steam in the reactant is 1:0.5˜10:1˜50.

11. The method of preparing 1,3-butadiene according to claim 8 , wherein, in (B), the oxidative dehydrogenation reaction is conducted at a reaction temperature of 300˜600° C. and at a liquid hourly space velocity of 1˜3 h −1 based on n-butene.

Assignments (7)
CHANGE OF ADDRESS Recorded Sep 2, 2022
From: SK GLOBAL CHEMICAL CO., LTD
To: SK GLOBAL CHEMICAL CO., LTD
Reel/Frame 061371/0328 →
CHANGE OF NAME Recorded Sep 2, 2022
From: SK GLOBAL CHEMICAL CO., LTD
To: SK GEO CENTRIC CO., LTD.
Reel/Frame 061371/0332 →
CORRECTIVE ASSIGNMENT TO CORRECT THE US APPLICATION SERIAL NUMBER UNDER WHICH THE ASSIGNMENT WAS PREVIOUSLY RECORDED ON REEL 026589 FRAME 0086. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT SHOULD HAVE BEEN RECORDED ON US APPLICATION NO. 12/746,558, AS NOTED ON THE ASSIGNMENT DOCUMENT. Recorded Jul 26, 2011
From: SK INNOVATION CO., LTD.
To: SK GLOBAL CHEMICAL CO., LTD. (FIFTY PERCENT OWNER); SK INNOVATION CO., LTD. (FIFTY PERCENT OWNER)
Reel/Frame 026653/0544 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 14, 2011
From: SK INNOVATION CO., LTD.
To: SK GLOBAL CHEMICAL CO., LTD. (FIFTY PERCENT OWNER); SK INNOVATION CO., LTD. (FIFTY PERCENT OWNER)
Reel/Frame 026589/0086 →
CHANGE OF NAME Recorded Jul 13, 2011
From: SK ENERGY CO., LTD.
To: SK INNOVATION CO., LTD.
Reel/Frame 026583/0336 →
CORRECTIVE ASSIGNMENT TO CORRECT THE COUNTRY NAME OF THE OFFICE ADDRESS OF THE ASSIGNEE (SK ENERGY CO., LTD.) PREVIOUSLY RECORDED ON REEL 024493 FRAME 0090. ASSIGNOR(S) HEREBY CONFIRMS THE COUNTRY OF THE OFFICE ADDRESS OF THE ASSIGNEE (SK ENERGY CO., LTD.) IS THE REPUBLIC OF KOREA. Recorded Jun 16, 2010
From: CHUNG, YOUNG MIN; KWON, YONG TAK; KIM, TAE JIN; LEE, SEONG JUN; KO, MIN SU; OH, SEUNG HOON; KIM, YONG SEUNG; SONG, IN KYU
To: SK ENERGY CO., LTD.
Reel/Frame 024543/0359 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 7, 2010
From: CHUNG, YOUNG MIN; KWON, YONG TAK; KIM, TAE JIN; LEE, SEONG JUN; KO, MIN SU; OH, SEUNG HOON; KIM, YONG SEUNG; SONG, IN KYU
To: SK ENERGY CO., LTD.
Reel/Frame 024493/0090 →