CN1157756A - Nanometre grade cobalt-manganese spinel and its manufacturing method and use - Google Patents

Nanometre grade cobalt-manganese spinel and its manufacturing method and use Download PDF

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Publication number
CN1157756A
CN1157756A CN96117198.7A CN96117198A CN1157756A CN 1157756 A CN1157756 A CN 1157756A CN 96117198 A CN96117198 A CN 96117198A CN 1157756 A CN1157756 A CN 1157756A
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China
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cobalt
manganese
citric acid
spinel
nitrate
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CN96117198.7A
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CN1049608C (en
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颜其洁
梁琦
陈开东
陈懿
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Nanjing University
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Nanjing University
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Abstract

A nm-grade Co-Mn spinel, which has chemical formula MnxCo3-xO4 (where X is greater than 0 but less than or equal to 1.4), average granularity less than 80 nm and specific surface area greater than 40 sq.m/g, is prepared through adding organic ligand to aqueous soltuion of cobolt nitrate and manganese nitrate, regulating pH value to 0-1.5, heating to 50-70 deg.C to form gel, baking, and calcine. Said Co-Mn spinel can be used as catalyst for hydrotransforming CO to hydrocarbon with high catalytic activity, selectivity and transform rate of CO.

Description

Nanometre grade cobalt-manganese spinel and method for making thereof and purposes
The present invention relates to the cobalt manganese composite oxide, specifically a kind of nano level cobalt-manganese spinel.
Cobalt-manganese spinel can [be seen N Yanamoto with the solution co-precipitation, J.Mat.Sci.Lett., 525,2.1983 and J L Martin de Vidales, Mat.Res.Bull., 1135,28,1993] and solid phase salt powder calcination method [see PRavindranathan, J.Solid state Chem., 20,66,1987] preparation spinel-type cobalt manganese composite oxide.But the lower (Mn of its manganese content of cobalt-manganese spinel with method for preparing xCo 3-xO 4, 0<x≤1) and particle diameter big (micron dimension), specific area is less<40m 2/ g) and particle diameter inhomogeneous, other dephasign is arranged, as catalyst, catalytic activity is relatively poor.
The object of the present invention is to provide a kind of nano level cobalt-manganese spinel, and easy method for making, a further object of the present invention provides its purposes as catalyst.
Technical scheme of the present invention is:
A kind of nanometre grade cobalt-manganese spinel, it consists of Mn xCo 3-xO 4, 0<x≤1.4 wherein, average grain diameter is less than 80nm, and specific area is greater than 40m 2/ g.
The method for making of cobalt-manganese spinel of the present invention adds organic ligand in cobalt nitrate, manganese nitrate aqueous solution, regulate PH to 0 to 1.5, forms gel at 50 to 70 ℃, oven dry, and roasting promptly gets nanometre grade cobalt-manganese spinel.
In cobalt nitrate, the manganese nitrate aqueous solution, the mol ratio of manganese ion and cobalt ions is x: 3-x, 0<x≤1.4, and the initial concentration of total metal ion (cobalt, manganese ion sum) is 0.3 to 0.9 mole.
The amount that organic ligand adds is that to make the metal ion (cobalt, manganese) and the mol ratio of organic ligand be 1: 1.
Organic ligand can be a citric acid, also can be the mixture of citric acid and acetylacetone,2,4-pentanedione.When selecting the mixture of citric acid and acetylacetone,2,4-pentanedione for use, the mol ratio of citric acid and acetylacetone,2,4-pentanedione is not less than 2: 1.After in cobalt nitrate, manganese nitrate aqueous solution, adding organic ligand, regulate pH value and place the formation gel at 50-70 ℃ to 0-1.5, with gel 100-120 ℃ of oven dry, then can roasting between 300-700 ℃ (preferred sintering temperature is 350-400 ℃), promptly get the single average grain diameter of crystalline phase less than 80nm, specific area is greater than 40m 2The nanometre grade cobalt-manganese spinel of the present invention of/g.
Nanometre grade cobalt-manganese spinel of the present invention can be used as catalyst, and it increases significantly for the activity of the general cobalt-manganese spinel of the specific activity of carbon monoxide hydrogenation (more than the particle diameter micron dimension).The olefine selective of the cobalt-manganese spinel of high Mn content is also apparently higher than the spinelle that hangs down manganese content.
Nanometre grade cobalt-manganese spinel of the present invention, its manganese content can be higher, and manganese, cobalt ions ratio can reach 1.4: 1.6.Average grain diameter is less than 80nm, epigranular, and specific area is greater than 40m 2/ g.As catalyst, bigger catalytic activity is arranged, for carbon monoxide hydrogenation, higher olefine selective is arranged.
By the following examples, further specify the present invention.
Embodiment 1. with raw material cobalt nitrate, manganese nitrate, acetylacetone,2,4-pentanedione, citric acid by Co: Mn: acetylacetone,2,4-pentanedione: the citric acid mol ratio is 2.5: 0.5: 0.5: 2.5 wiring solution-formings, the initial concentration that makes total metal ion in the solution is at 0.6M, with nitric acid regulator solution initial p H value 0, in 60 ℃ of water-baths, form gel, gel 110 ℃ of oven dry, was got Mn in 2 hours in 350 ℃ of roastings again 0.5Co 2.5O 4Sample.Its average grain diameter is 10-15nm, specific area 74m 2/ g, epigranular.
Embodiment 2. with raw material cobalt nitrate, manganese nitrate, acetylacetone,2,4-pentanedione, citric acid by Co: Mn: acetylacetone,2,4-pentanedione: the citric acid mol ratio is 2.0: 1.0: 0.5: 2.5 wiring solution-formings, the initial concentration that makes total metal ion in the solution is at 0.6M, with nitric acid regulator solution initial p H value 0, in 60 ℃ of water-baths, form gel, gel 110 ℃ of oven dry, was got Mn in 2 hours in 350 ℃ of roastings again 1.0Co 2.0O 4Sample.Its average grain diameter is 10-15nm, specific area 71m 2/ g, epigranular.
Embodiment 3. with raw material cobalt nitrate, manganese nitrate, acetylacetone,2,4-pentanedione, citric acid by Co: Mn: acetylacetone,2,4-pentanedione: the citric acid mol ratio is 1.8: 1.2: 0.5: 2.5 wiring solution-formings, the initial concentration that makes total metal ion in the solution is at 0.6M, with ammoniacal liquor regulator solution initial p H value 1, in 60 ℃ of water-baths, form gel, gel 110 ℃ of oven dry, was got Mn in 2 hours in 350 ℃ of roastings again 1.2Co 1.8O 4Sample.Its average grain diameter is 10-15nm, specific area 78m 2/ g, epigranular.
Embodiment 4. with raw material cobalt nitrate, manganese nitrate, acetylacetone,2,4-pentanedione, citric acid by Co: Mn: acetylacetone,2,4-pentanedione: the citric acid mol ratio is 2.0: 1.0: 0.5: 2.5 wiring solution-formings, the initial concentration that makes total metal ion in the solution is at 0.4M, with ammoniacal liquor regulator solution initial p H value 1.5, in 60 ℃ of water-baths, form gel, gel 110 ℃ of oven dry, was got MnCo in 2 hours in 350 ℃ of roastings again 2O 4Sample.Its average grain diameter is 10-15nm, specific area 71m 2/ g, epigranular.
Embodiment 5. with raw material cobalt nitrate, manganese nitrate, acetylacetone,2,4-pentanedione and citric acid by Co: Mn: acetylacetone,2,4-pentanedione: the citric acid mol ratio is 2.0: 1.0: 0.5: 2.5 wiring solution-formings, the initial concentration that makes total metal ion in the solution is at 0.8M, solution initial PH value is 0.5, in 60 ℃ of water-baths, form gel, gel 110 ℃ of oven dry, was got MnCo in 2 hours in 400 ℃ of roastings again 2O 4Sample.Its average grain diameter is 10-15nm, specific area 70m 2/ g, epigranular.
Embodiment 6. with raw material cobalt nitrate, manganese nitrate, citric acid by Co: Mn: the citric acid mol ratio is 2.0: 1.0: 3.0 wiring solution-formings, the initial concentration that makes total metal ion in the solution is at 0.6M, with nitric acid regulator solution initial p H value 0, in 60 ℃ of water-baths, form gel, gel 110 ℃ of oven dry, was got MnCo in 2 hours in 350 ℃ of roastings again 2O 4Sample.Its average grain diameter is 10-15nm, specific area 40m 2/ g, epigranular.
Embodiment 7. cobalt-manganese spinel MnCo of the present invention 2O 4As the carbon monoxide hydrogenation catalyst: reaction condition: 300 ℃ of temperature, pressure 1atm, H 2/ CO (vol/vol)=2.0 GHSV 700/h, the conversion ratio of carbon monoxide is 17.4%, C 2-C 4Olefine selective is 40%.(the micron dimension MnCo of prior art 2O 4, the conversion ratio of CO is 9.6% under the similarity condition).
Embodiment 8. cobalt-manganese spinel Mn of the present invention 1.2Co 1.8O 4As the carbon monoxide hydrogenation catalyst: reaction condition: 270 ℃ of temperature, pressure 1atm, H 2/ CO (vol/vol)=2.0 GHSV 700/h, the conversion ratio of carbon monoxide is 13.2%, C 2-C 4Olefine selective is 43.2%.(prior art can't obtain Mn: Co>1: 2 cobalt-manganese spinel).

Claims (7)

1. a nanometre grade cobalt-manganese spinel is characterized in that it consists of Mn xCo 3-xO 4, 0<x≤1.4 wherein, average grain diameter is less than 80nm, and specific area is greater than 40m 2/ g.
2. the method for making of cobalt-manganese spinel according to claim 1 is characterized in that adding organic ligand in cobalt nitrate, manganese nitrate aqueous solution, regulates PH to 0 to 1.5, forms gel at 50 to 70 ℃, oven dry, and roasting promptly gets nanometre grade cobalt-manganese spinel.
3. preparation method according to claim 2 is characterized in that in cobalt nitrate, the manganese nitrate aqueous solution that the mol ratio of manganese ion and cobalt ions is x: 3-x, 0<x≤1.4, and the initial concentration of total metal ion is 0.3 to 0.9 mole.
4. preparation method according to claim 2, the mol ratio that it is characterized in that metal ion and organic ligand is 1: 1.
5. preparation method according to claim 2 is characterized in that organic ligand is the mixture of citric acid or citric acid and acetylacetone,2,4-pentanedione.
6. preparation method according to claim 5 is characterized in that the mol ratio of citric acid and acetylacetone,2,4-pentanedione is not less than 2: 1 in organic ligand citric acid and the acetylacetone,2,4-pentanedione mixture.
7. the purposes of cobalt-manganese spinel according to claim 1 is characterized in that being used as the catalyst that co hydrogenation is converted into hydrocarbon reaction.
CN96117198A 1996-12-02 1996-12-02 Nanometre grade cobalt-manganese spinel and its manufacturing method and use Expired - Fee Related CN1049608C (en)

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100427380C (en) * 2005-06-08 2008-10-22 北京化工大学 Process for preparing high radio surface area nano spinel by lamellar precursor body method
CN101670999B (en) * 2009-09-27 2012-04-11 中国科学院上海硅酸盐研究所 Mn-Co-doped spinel composite nanometer material and low-temperature sintering method thereof
CN103073072A (en) * 2013-01-29 2013-05-01 安泰科技股份有限公司 Manganese cobalt composite oxide (MnCo2O4) magnetic nanocrystal and preparation method thereof
CN103746104A (en) * 2013-12-09 2014-04-23 中国科学院福建物质结构研究所 Manganese cobalt oxide self-assembled micro-spheres, and preparation and applications thereof
CN104810518A (en) * 2015-04-15 2015-07-29 南开大学 Cobalt-manganese-based spinel nano material as well as preparation method and application thereof
CN105170158A (en) * 2015-07-22 2015-12-23 重庆工商大学 CoMn composite oxide catalyst for eliminating benzene-serial volatile organic compounds in air and preparation method for therefor
CN105555922A (en) * 2013-07-31 2016-05-04 沙特基础工业公司 A process for the production of olefins through fischer-tropsch based synthesis
CN108264093A (en) * 2018-01-09 2018-07-10 上海应用技术大学 A kind of preparation method of cobalt-manganese spinel microballoon
CN108682869A (en) * 2018-04-10 2018-10-19 云南铝业股份有限公司 Manganese cobalt spinel oxygen reduction catalyst and preparation method thereof

Family Cites Families (3)

* Cited by examiner, † Cited by third party
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JP2831745B2 (en) * 1989-10-31 1998-12-02 富士通株式会社 Semiconductor device and manufacturing method thereof
US5248701A (en) * 1991-08-05 1993-09-28 Exxon Research And Engineering Company Substituted cobalt catalysts for Fischer-Tropsch synthesis
CN1029510C (en) * 1991-11-22 1995-08-16 中国科学院山西煤炭化学研究所 Preparing method for hydrogen refining cobalt molybdenum catalyzer.

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100427380C (en) * 2005-06-08 2008-10-22 北京化工大学 Process for preparing high radio surface area nano spinel by lamellar precursor body method
CN101670999B (en) * 2009-09-27 2012-04-11 中国科学院上海硅酸盐研究所 Mn-Co-doped spinel composite nanometer material and low-temperature sintering method thereof
CN103073072A (en) * 2013-01-29 2013-05-01 安泰科技股份有限公司 Manganese cobalt composite oxide (MnCo2O4) magnetic nanocrystal and preparation method thereof
CN103073072B (en) * 2013-01-29 2014-08-13 安泰科技股份有限公司 Manganese cobalt composite oxide (MnCo2O4) magnetic nanocrystal and preparation method thereof
CN105555922A (en) * 2013-07-31 2016-05-04 沙特基础工业公司 A process for the production of olefins through fischer-tropsch based synthesis
CN103746104A (en) * 2013-12-09 2014-04-23 中国科学院福建物质结构研究所 Manganese cobalt oxide self-assembled micro-spheres, and preparation and applications thereof
CN104810518A (en) * 2015-04-15 2015-07-29 南开大学 Cobalt-manganese-based spinel nano material as well as preparation method and application thereof
CN104810518B (en) * 2015-04-15 2017-03-08 南开大学 A kind of cobalt manganese systems spinel nano material and its preparation method and application
CN105170158A (en) * 2015-07-22 2015-12-23 重庆工商大学 CoMn composite oxide catalyst for eliminating benzene-serial volatile organic compounds in air and preparation method for therefor
CN105170158B (en) * 2015-07-22 2018-02-27 重庆工商大学 Eliminate CoMn composite oxide catalysts of benzene in air system volatile organic matter and preparation method thereof
CN108264093A (en) * 2018-01-09 2018-07-10 上海应用技术大学 A kind of preparation method of cobalt-manganese spinel microballoon
CN108682869A (en) * 2018-04-10 2018-10-19 云南铝业股份有限公司 Manganese cobalt spinel oxygen reduction catalyst and preparation method thereof

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