Abstract:
The present invention relates to: a catalyst for glycerin dehydration; a preparation method therefor; and an acrolein preparation method using the catalyst. According to one embodiment of the present invention, the catalyst is used in glycerin dehydration so as to exhibit high catalytic activity, a high yield and high acrolein selectivity, and has a characteristic in which carbon is not readily deposited, thereby having a long lifetime compared with that of a conventional catalyst.
Abstract:
A PROCESS FOR MANUFACTURING CONJUGATED DIOLEFINS FROM AN ALKYL-1,3-DIOZANE WHICH COMPRISES PASSING SAID DIOXANE, AT A TEMPERATURE OF ABOUT 250 TO 500* C., OVER A CATALYST COMPRISING A COMPOUND OF AN ELEMENT SELECTED FROM GROUPS II-A AND II-B OF THE PERIODIC TABLE AND A PRECURSOR OF PHOSPHORIC ANHYDRIDE DEPOSITED ON A SILICA CARRIER, THE GROUP II-A AND GROUP II-B ELEMENT, EXPRESSED AS THE OXIDE, BEING PRESENT IN AN AMOUNT OF ABOUT 2 TO 20% BY WEIGHT, BASED ON THE TOTAL CATALYST AND THE PHOSPHORIC ANHYDRIDE PRECURSOR, EXPRESSED AS P2/5, BEING PRESENT IN AN AMOUNT OF ABOUT 2 TO 20% BY WEIGHT, BASED ON THE TOTAL CATALYST, THE MOLAR RATIO OF P2O5 TO THE GROUPS II-A AND II-B METAL OXIDE BEING ABOUT 0.1 TO 0.6, SAID PROCESS BEING CONDUCTED IN THE PRESENT OF A STEAM DILUENT HAVING A PHOSPHORIC ACID CONTENT OF ABOUT 0.001 TO 0.1% BY WEIGHT, EXPRESSED AS P2O5, THE RATIO BY VOLUME OF WATER TO THE DIOXANE, CALCULATED IN THE LIQUID STATE BEING ABOUT 0.1 TO 15, AND RECOVERING THE CONJUGATED DIOLEFINS.
Abstract:
The present disclosure relates to a catalyst for dehydration of glycerin, a preparation method thereof, and a production method of acrolein using the catalyst.Particularly, the catalyst according to an embodiment of the present disclosure is used in a dehydration reaction of glycerin to exhibit high catalytic activity, a high yield, and high selectivity to acrolein and acrylic acid, and has a longer lifetime compared to the conventional catalysts due to a characteristic that coke carbon cannot be easily deposited on the surface of the catalyst.
Abstract:
Novel catalytic compositions for cracking of crude oil fractions are disclosed. The catalytic compositions comprise a basic material. When used in a cracking process, preferably a FCC process, the resulting LCO and HCO fractions have desirably low aromatics levels. Further disclosed is a one-stage FCC process using the catalytic composition of the invention. Also disclosed is a two-stage FCC process for maximizing the LCO yield.
Abstract:
Disclosed is a method for producing an α,β-unsaturated ether efficiently and stably for a long time. In the method for producing an α,β-unsaturated ether, an acetal is thermally decomposed in the presence of a catalyst containing an apatite represented by any of the following formula (1)-(4) (M)5−y(HZO4)y(ZO4)3−y(X)1−y (1) (M)5−y(HPO4)y(PO4)3−y(X)1−y (2) (M)5−y+2n(HZO4)y(ZO4)3−y(X)1−y(SiO4)n (3) (M)5−y+m(HZO4)y(ZO4)3−y(X)1−y(CO3)m (4).
Abstract:
The catalytic oxidative dehydrogenation of at least one dehydrogenatable organic compound which has at least one ##STR1## grouping is carried out in the presence of a zinc titanate catalyst. The selectivity of the zinc titanate catalyst may be improved by a promoter at least one member of which is selected from the group consisting of chromium, antimony, bismuth, aluminum, phosphorus, indium, tin, lanthanum and cerium.