![]() ![]() ![]() A process according to claim 9 in which the feedstock is contacted with the catalyst in the presence of hydrogen under isomerization conditions of a temperature from 400° C. to 540° C., a pressure from atmospheric to 25,000 kPa and a space velocity (LHSV) from 0.1 to 20 hr. A process according to claim 1 in which the feedstock is contacted with the catalyst in the pressure of hydrogen under isomerization conditions of a temperature from 200° C. A process according to claim 1 in which the feedstock is contacted with the catalyst in the absence of added hydrogen.ĩ. ![]() A process according to claim 6 in which the hydrogenation component comprises platinum.Ĩ. A process according to claim 1 in which the hydrogenation component comprises a noble metal of Group VIIIA of the Periodic Table.ħ. A process according to claim 1 in which the zeolite beta has a silica:alumina ratio of at least 250:1.Ħ. A process according to claim 1 in which the zeolite beta has a silica:alumina ratio over 100:1.ĥ. A process according to claim 2 in which the proportion of aromatic components is from 10 to 50 weight percent of the feedstock.Ĥ. A process according to claim 1 in which the feedstock includes aromatic components in addition to the straight chain paraffins.ģ. ![]() A process for dewaxing a hydrocarbon feedstock containing straight chain paraffins, which comprises contacting the feedstock with a catalyst comprising zeolite beta having a silica:alumina ratio of at least 30:1 and a hydrogenation component under isomerization conditions.Ģ. ![]()
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