Manufacture of butadiene from ethylene
View Patent ↗A method of producing butadiene includes: (1) dimerizing ethylene to butene followed by (2) oxidatively dehydrogenating the butene to butadiene and (3) recovering the butadiene by (i) absorbing the product with a hydrocarbon absorber oil and (ii) stripping a crude product stream from the absorber oil. The absorber oil is selected so as to be effective to sequester ethylene dimerization-derived impurities from the system.
1. A method of producing butadiene from an ethylene raw material feed comprising:
providing ethylene to a homogeneous reaction medium housed in a dimerization reactor;
dimerizing ethylene to butene in the homogeneous reaction medium to provide a hydrocarbonaceous butene rich feed with ethylene dimerization-derived impurities therein, wherein said ethylene dimerization-derived impurities include one or more impurities selected from ethylene trimers (C6); ethylene tetramers (C8); diolefins comprising one or more of butadiene, isoprene, and heavier diolefins; as well as acetylenic by-products of ethylene dimerization and wherein the hydrocarbonaceous butene rich feed has greater than 100 ppm of said ethylene dimerization-derived impurities;
mixing said hydrocarbonaceous butene rich feed with steam and an oxygen rich gas to form an oxidative dehydrogenation reactor feed stream and superheating said oxidative dehydrogenation reactor feed stream to a temperature of at least 204° C. (400° F.),
feeding the oxidative dehydrogenation reactor feed stream to an oxidative dehydrogenation reactor;
oxidatively dehydrogenating said reactor feed stream in the oxidative dehydrogenation a reactor over an oxidative dehydrogenation catalyst thereby forming a butadiene enriched product stream;
feeding the butadiene enriched product stream to a C4 absorber wherein C4's including butadiene and ethylene dimerization-derived impurities in the oxidative dehydrogenation reactor effluent are absorbed into a compatible absorption oil;
providing the absorption oil to a stripper in which C4 volatiles including butadiene are desorbed and stripped from said absorption oil to provide a crude product stream; and
recovering butadiene from said crude product stream.
2. The method according to claim 1 , wherein the hydrocarbonaceous butene-rich feed has greater than 200 ppm of ethylene dimerization-derived impurities.
3. The method according to claim 1 , wherein the hydrocarbonaceous butene-rich feed has greater than 300 ppm of ethylene dimerization-derived impurities.
4. The method according to claim 1 , wherein the hydrocarbonaceous butene-rich feed has greater than 100 ppm of ethylene dimerization-derived impurities and less than 1% by weight ethylene dimerization-derived impurities.
5. The method according to claim 1 , wherein the absorber oil comprises one or more compounds selected from the group consisting of toluene, xylenes, styrene and naphthalenes.
6. The method according to claim 1 , wherein the absorber oil contains over 90% paraffinic compounds.
7. The method according to claim 1 , wherein the absorber oil contains 90% by weight or more of compounds with atmospheric pressure boiling points of from 75° C. to 250° C.
8. The method according to claim 1 , wherein the absorber contains 90% by weight or more of an aromatic naphtha product with an atmospheric pressure boiling range of from 90° C. to 150° C.
9. The method according to claim 1 , wherein the absorber oil contains 90% by weight or more of vinyl cyclohexene.
10. A method of co-producing butene-1 and butadiene from an ethylene raw material feed comprising:
providing ethylene to a homogeneous reaction medium including a homogeneous titanium-aluminum catalyst housed in a dimerization reactor;
dimerizing ethylene predominantly to butene-1 in the homogeneous reaction medium to provide (i) a hydrocarbonaceous butene-1 rich feed with ethylene dimerization-derived impurities therein, wherein said ethylene dimerization-derived impurities include one or more impurities selected from ethylene trimers (C6); ethylene tetramers (C8); diolefins comprising one or more of butadiene, isoprene, and heavier diolefins; as well as acetylenic by-products of ethylene dimerization and wherein the hydrocarbonaceous butene-1 rich feed has greater than 100 ppm of said ethylene dimerization-derived impurities and (ii) a butene-1 rich product stream;
withdrawing and purifying the butene-1 rich product stream and recovering butene-1 therefrom;
mixing said hydrocarbonaceous butene-1 rich feed with steam and an oxygen rich gas to form an oxidative dehydrogenation reactor feed stream and superheating said oxidative dehydrogenation reactor feed stream to a temperature of at least 204° C. (400° F.),
feeding the oxidative dehydrogenation reactor feed stream to an oxidative dehydrogenation reactor;
oxidatively dehydrogenating said reactor feed stream in the oxidative dehydrogenation reactor over an oxidative dehydrogenation catalyst thereby forming a butadiene enriched product stream;
feeding the butadiene enriched product stream to a C4 absorber wherein C4's including butadiene and ethylene dimerization-derived impurities which may be present in oxidative dehydrogenation reactor effluent, are absorbed into a compatible absorption oil;
providing the absorption oil to a stripper in which C4 volatiles including butadiene are desorbed and stripped from said absorption oil to provide a crude product stream; and
recovering butadiene from said crude product stream.
11. The method according to claim 10 , wherein the homogeneous titanium-aluminum catalyst comprises a titanium organometallic complex with at least one alkoxide ligand and an alkyl aluminum co-catalyst.
12. The method according to claim 10 , wherein the homogeneous titanium-aluminum catalyst comprises titanium tetrabutoxide and triethyl aluminum.