Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
169 words
In a process for dehydrogenating a hydrocarbon charge stock, consisting essentially of normal paraffins having from about 3 to about 20 carbon atoms per molecule to form linear mono-olefins the sequential steps of: (a) reacting said charge stock in the presence of hydrogen, in a dehydrogenation reaction zone, at dehydrogenation conditions selected to convert paraffinic hydrocarbons to linear mono-olefinic hydrocarbons; (b) separating the resulting dehydrogenation zone effluent, in a first separation zone, at separating conditions to provide (1) a hydrogen-rich, principally vaporous phase containing olefinic hydrocarbons and, (2) a second phase containing linear mono-olefinic hydrocarbons and unreacted normal paraffins; (c) separating said second phase, in a second separation zone to (1) recover said linear mono-olefinic hydrocarbons, and (2) provide a normal paraffin concentrate containing olefinic hydrocarbons; (d) reacting at least a portion of said hydrogen-rich vaporous phase, in a hydrotreating zone, at hydrotreating conditions selected to saturate the olefinic hydrocarbons therein; and, (e) introducing the resulting substantially olefin-free effluent from said hydrotreating reaction zone into said dehydrogenation reaction zone.
Claim 2
Dependent Claim
169 words
In a process for dehydrogenating a hydrocarbon charge stock, consisting essentially of normal paraffins having from about 3 to about 20 carbon atoms per molecule to form linear mono-olefins the sequential steps of: (a) reacting said charge stock in the presence of hydrogen, in a dehydrogenation reaction zone, at dehydrogenation conditions selected to convert paraffinic hydrocarbons to linear mono-olefinic hydrocarbons; (b) separating the resulting dehydrogenation zone effluent, in a first separation zone, at separating conditions to provide (1) a hydrogen-rich, principally vaporous phase containing olefinic hydrocarbons and, (2) a second phase containing linear mono-olefinic hydrocarbons and unreacted normal paraffins; (c) separating said second phase, in a second separation zone to (1) recover said linear mono-olefinic hydrocarbons, and (2) provide a normal paraffin concentrate containing olefinic hydrocarbons; (d) reacting at least a portion of said hydrogen-rich vaporous phase, in a hydrotreating zone, at hydrotreating conditions selected to saturate the olefinic hydrocarbons therein; and, (e) introducing the resulting substantially olefin-free effluent from said hydrotreating reaction zone into said dehydrogenation reaction zone.
Claim 3
Dependent Claim
23 words
The process of claim 1 further characterized in that said normal paraffin concentrate, containing olefinic hydrocarbons is introduced into said hydrotreating reaction zone.
Claim 4
Dependent Claim
24 words
The process of claim 1 further characterized in that at least a portion of said charge stock is introduced into said hydrotreating reaction zone.
Claim 5
Dependent Claim
24 words
The process of claim 1 further characterized in that said charge stock normal paraffins contain from 6 to about 10 carbon atoms per molecule.
Claim 6
Dependent Claim
24 words
The process of claim 1 further characterized in that said charge stock normal paraffins contain from 11 to about 18 carbon atoms per molecule.
Claim 7
Dependent Claim
27 words
The process of claim 1 further characterized in that said second separation zone in an adsorption-separation zone having disposed therein a zeolitic crystalline aluminosilicate molecular sieve adsorbent.
Claim 8
Dependent Claim
30 words
The process of claim 1 further characterized in that said dehydrogenation reaction zone has disposed therein a non-acid acting catalytic composite containing at least one Group VIII noble metal component.
Claim 9
Dependent Claim
30 words
The process of claim 1 further characterized in that said hydrotreating reaction zone has disposed therein a non-acid acting catalytic composite containing at least one Group VIII noble metal component.
Claim 10
Dependent Claim
25 words
The process of claim 6 further characterized in that said adsorbent is selected from the group consisting of type X and type Y structured zeolites.
Claim 11
Dependent Claim
26 words
The process of claim 9 further characterized in that said zeolite contains at least one metal cation from the metals of Groups I-A, II-A and I-B.