Process for N-butanizing field butane feedstock to thermal crackers
AssigneeSabic Global Technologies B.V.
InventorsVijay Dinkar Bodas, Sultan Al-Otaibe, Guillermo Leal, Mohammed Bismillah Ansari
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Abstract
Described is a process for producing field butane. The process includes increasing the n-butane concentration in field butane. The process may include a concentration process that includes distillation and a thermal cracking process.
Claims19
A method of increasing n-butane concentration in field butane, the method comprising:
- subjecting a feed stream, comprising primarily n-butane and isobutane collectively, to a concentrating process, the concentrating process comprising distilling the feed stream in one or more distillation columns to produce a first product stream comprising primarily n-butane and a second product stream comprising methane, ethane, and propane;
- and
- cracking, in a thermal cracker, the first product stream to produce a third product stream comprising primarily ethylene and a fourth product stream comprising primarily n-butane;
- and
- recycling, from the thermal cracker, at least some of the fourth product stream to the one or more distillation columns;
- wherein the concentrating process comprises:
- distilling, in a first distillation column, a combined stream that comprises a mixture of the feed stream and a recycle stream comprising primarily isobutane to produce a bottoms stream comprising primarily n-pentane, an intermediate stream comprising primarily n-butane, and an overhead stream comprising primarily isobutane;
- combining the intermediate stream and the bottoms stream to produce the first product stream;
- isomerizing the overhead stream in a reactor to convert at least some of the isobutane in the overhead stream to n-butane;
- and
- distilling effluent from the reactor, in a second distillation column, to form the recycle stream and the second product stream.
The method of 1, wherein the feed stream comprises 62 mol. % to 72 mol. % n-butane and 24 mol. % to 34 mol. % isobutene and wherein the first product stream comprises 85 mol. % to 95 mol. % n-butane.
The method of 1, wherein the feed stream comprises 94 mol. % to 98 mol. % n-butane and isobutane collectively.
The method of 1, wherein the feed stream further comprises n-pentane.
The method of 1, wherein the second product stream further comprises 5 mol. % to 15 mol. % methane, 15 mol. % to 25 mol. % ethane, and 65 mol. % to 75 mol. % propane.
Dependencies are inferred from the claim text.