Carbon nitride heterogeneous catalyst containing rhodium, method for preparing the same, and method for preparing acetic acid using the same
US-2018147565-A1 · May 31, 2018 · US
US10196339B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10196339-B2 |
| Application number | US-201515540857-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 24, 2015 |
| Priority date | Dec 29, 2014 |
| Publication date | Feb 5, 2019 |
| Grant date | Feb 5, 2019 |
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This invention relates to a catalyst used in a carbonylation of methanol using carbon monoxide to acetic acid, and more particularly to a heterogeneous catalyst represented by Rh/WxC (where x is an integer of 1 or 2) in which a complex of a rhodium compound and 3-benzoylpyridine is fixed on a support of tungsten carbide.
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The invention claimed is: 1. A method of preparing a heterogeneous catalyst, comprising: (S1) preparing a tungsten carbide support powder by thermally treating a tungsten carbide gel including a tungsten precursor, a carbon precursor and a silica molecular sieve template to a temperature of 800 to 1000° C. in presence of a gas mixture comprising hydrogen gas and nitrogen gas so as to harden a surface thereof and then by extracting and removing the silica molecular sieve template; (S2) preparing a complex by reacting a rhodium compound with 3-benzoylpyridine; and (S3) preparing a heterogeneous catalyst represented by Rh/WxC (wherein x is an integer of 1 or 2) by fixing the complex prepared in (S2) on the tungsten carbide support prepared in (S1). 2. The method of claim 1 , wherein the thermally treating in (S1) is performed in the presence of the gas mixture including hydrogen gas and nitrogen gas through gradual heating under temperature gradient conditions in a manner in which a reaction temperature is increased to 250 to 300° C. from room temperature at a heating rate of 1 to 3° C./min, maintained for 3 to 7 hr, further increased to 550 to 650° C. at a heating rate of 1 to 3° C./min, maintained for 3 to 7 hr, additionally increased to 800 to 1000° C. at a heating rate of 1 to 3° C./min, and maintained for 3 to 7 hr. 3. The method of claim 1 , wherein the silica molecular sieve is selected from a group consisting of SBA-15, MCM-41, and FSM-16. 4. The method of claim 1 , wherein the tungsten carbide support prepared in (S1) has a pore structure having an average pore size of 3 to 10 nm, with a specific surface area of 10 to 200 m 2 /g. 5. The method of claim 1 , wherein the rhodium compound used in (S2) is dichloro tetracarbonyl dirhodium (C 4 O 4 Cl 42 Rh 2 ). 6. The method of claim 1 , wherein in (S3), the complex is fixed in an amount of 3 to 30 wt % based on a total weight of the tungsten carbide support.
the impregnation liquid containing organic compounds · CPC title
Operations & Transport · mapped topic
Cross-Sectional Technologies · mapped topic
Addition of a binding agent or of material, later completely removed among others as result of heat treatment, leaching or washing,(e.g. forming of pores; protective layer, desintegrating by heat) · CPC title
Rhodium · CPC title
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