PREPARATION METHOD OF PLATINUM/TIN/ALUMINA CATALYST FOR DIRECT DEHYDROGENATION OF n-BUTANE AND METHOD FOR PRODUCING C4 OLEFINS USING SAID CATALYST
The provided is a preparation method of a platinum/tin/alumina catalyst which comprises platinum as an active component having high activity to direct dehydrogenation of n-butane, tin capable of preventing platinum particles from being sintered and maintaining a size of the platinum particles to be small, thereby improving dispersibility and increasing an amount at an active site during the dehydrogenation and also capable of suppressing carbon deposition, thereby increasing stability of the catalyst, and as an support for supporting them, an alumina support which is known as being suitable for direct dehydrogenation of n-butane and is capable of maintaining high dispersibility of the platinum with high thermal and mechanical stability, and a method for producing high value-added C4 olefins through direct dehydrogenation of inexpensive n-butane by using the catalyst prepared by the preparation method.
1 . A preparation method of a platinum/tin/alumina catalyst for direct dehydrogenation of n-butane, comprising the following steps:
(a) preparing a tin precursor solution by dissolving a tin precursor and an acid in a first solvent;
(b) impregnating the tin precursor solution on a basic alumina support;
(c) obtaining tin/alumina in which tin is impregnated on the alumina support by heat drying and heat treating a product obtained from the step (b);
(d) preparing a platinum precursor solution by dissolving a platinum precursor in a second solvent;
(e) impregnating the platinum precursor solution on the tin/alumina prepared in the step (c); and
(f) obtaining a platinum/tin/alumina catalyst by heat drying and heat treating a product obtained from the step (e).
2 . The method of claim 1 , wherein the tin precursor used in the step (a) includes at least one selected from a group consisting of tin chloride, tin nitride, tin bromide, tin oxide and tin acetate.
3 . The method of claim 1 , wherein an amount of the tin precursor used in the step (a) is 0.5 to 10 wt % based on a total weight of the final platinum/tin/alumina catalyst.
4 . The method of claim 1 , wherein the acid used in the step (a) includes at least one selected from the group consisting of a hydrochloric acid, a nitric acid, a sulfuric acid, a hydrofluoric acid and a phosphoric acid.
5 . The method of claim 1 , wherein each of the first solvent and the second solvent respectively used in the step (a) and the step (d) is water or alcohol.
6 . The method of claim 1 , wherein in the step (c), the heat drying is carried out at a temperature of 50 to 200° C. and the heat treating is carried out at a temperature of 350 to 1000° C.
7 . The method of claim 1 , wherein the platinum precursor used in the step (d) includes at least one selected from a group consisting of chloroplatinic acid, platinum oxide, platinum chloride and platinum bromide.
8 . The method of claim 1 , wherein in the step (f), the heat drying is carried out at a temperature of 50 to 200° C. and the heat treating is carried out at a temperature of 400 to 800° C.
9 . A method for producing C4 olefins through direct dehydrogenation of n-butane by using a mixed gas containing n-butane and nitrogen as a reactant on the platinum/tin/alumina catalyst prepared by a method of any one of claims 1 to 8 .
10 . The method of claim 9 , wherein the direct dehydrogenation of n-butane is carried out at a temperature of 300 to 800° C.
11 . The method of claim 9 , wherein the mixed gas has a volume ratio of the n-butane to the nitrogen is 1:0.2 to 10.
12 . The method of claim 9 , wherein an injection amount of the mixed gas is set to have a weight hourly space velocity of 10 to 6000 cc·hr −1 ·gcat −1 with respect to the n-butane.