Flexible manufacturing system for selectively producing different linear alpha olefins
A flexible manufacturing system for selectively producing different alpha-olefins from ethylene includes: (a) a reaction section 18 with ethylene feed operative to oligomerize ethylene; (b) a catalyst feed system 12, 14, 16 comprising a plurality of independent homogeneous catalyst feeders connected with the reaction section for alternatively providing different selective homogeneous catalyst compositions to the reaction section; (c) an ethylene recycle column 22 coupled to the reaction section and adapted to receive crude product and unreacted ethylene therefrom, the recycle column being operative to separate ethylene and optionally lower oligomers from the crude product which are recycled to the ethylene feed to the reaction section, the ethylene recycle column being further operative to provide a crude product bottoms stream; (d) a catalyst removal section 20 coupled to the reaction section adapted to remove spent catalyst from the system; and (e) a first product separation column 24 connected to the recycle column receiving the crude product stream therefrom, the product separation column being operative to separate purified oligomer from the crude product stream. Optionally provided is a second product separation column 26.
1. A flexible manufacturing system for selectively producing different alpha-olefins from ethylene comprising:
(a) a reaction section with ethylene feed operative to oligomerize ethylene;
(b) a catalyst feed system comprising a plurality of independent homogeneous catalyst feeders connected with the reaction section for alternatively providing different selective homogeneous catalyst compositions to the reaction section;
(c) an ethylene recycle column coupled to the reaction section and adapted to receive crude product and unreacted ethylene therefrom, the recycle column being operative to separate ethylene and optionally lower oligomers from the crude product which are recycled to the ethylene feed to the reaction section, the ethylene recycle column being further operative to provide a crude product bottoms stream;
(d) a catalyst removal section coupled to the reaction section adapted to remove spent catalyst from the system; and
(e) a first product separation column connected to the recycle column receiving the crude product stream therefrom, the product separation column being operative to separate purified oligomer from the crude product stream.
2. The flexible manufacturing system for selectively producing different alpha-olefins according to claim 1 , wherein one of the homogeneous catalyst feeds is provided a first homogeneous catalyst composition comprising a titanate catalyst and an organo aluminum cocatalyst, the first homogeneous catalyst composition being selective for 1-butene.
3. The flexible manufacturing system for selectively producing different alpha-olefins according to claim 1 , wherein one of the homogeneous catalyst feeders is provided a second homogeneous catalyst composition comprising a chromium catalyst and an organoaluminum cocatalyst, the second homogeneous catalyst composition being selective for 1-hexene.
4. The flexible manufacturing system for selectively producing different alpha-olefins according to claim 3 , wherein a magnesium compound cocatalyst is also provided to the catalyst feeders.
5. The flexible manufacturing system for selectively producing different alpha-olefins according to claim 3 , wherein one of the homogeneous catalyst feeders is provided a third homogeneous catalyst composition comprising a chromium catalyst, a phosphino amine cocatalyst and an organoaluminum cocatalyst, the third homogeneous catalyst composition being selective for 1-octene and 1-hexene.
6. The flexible manufacturing system for selectively producing different alpha-olefins according to claim 1 , wherein the first product separation column is connected to provide bottoms to the catalyst feed system as solvent for homogeneous catalyst compositions.
7. The flexible manufacturing system for selectively producing different alpha-olefins according to claim 1 , further comprising a second product separation column coupled to the first product separation column to receive bottoms therefrom and separate the bottoms from the first column into an overhead oligomerized product stream and a bottoms stream.
8. The flexible manufacturing system for selectively producing different alpha-olefins according to claim 7 , wherein the second product separation column is connected to provide bottoms to the catalyst feed system as solvent for homogeneous catalyst compositions.
9. The flexible manufacturing system for selectively producing different alpha-olefins according to claim 1 , operated with a homogeneous catalyst composition comprising a titanate catalyst and organoaluminum cocatalyst selective for 1-butene, wherein selectivity to 1-butene is at least 85 weight % based on ethylene consumption.
10. The flexible manufacturing system for selectively producing different alpha-olefins according to claim 1 , operated with a homogeneous catalyst composition comprising a chromium catalyst and an organoaluminum cocatalyst selective for 1-hexene, wherein selectivity to 1-hexene is at least 75 weight % based on ethylene consumption.
11. The flexible manufacturing system for selectively producing different alpha-olefins according to claim 1 , further comprising a second product separation column coupled to the first product separation column to receive bottoms therefrom and separate the bottoms from the first column into an overhead oligomeric product stream and a bottom stream and operated with a homogeneous catalyst composition comprising a chromium catalyst, a phosphino amine cocatalyst, and an organoaluminum cocatalyst, the catalyst being selective for 1-octene and 1-hexene, wherein 1-hexene is withdrawn as a product from the overhead of the first product separation column and 1-octene is withdrawn as a product from the second product separation column and wherein selectivity to 1-octene is at least 65 weight % based on ethylene consumption and selectivity to 1-hexene and 1-octene collectively is at least 85 weight % based on ethylene consumption.
12. The flexible manufacturing system for selectively producing different alpha-olefins according to claim 1 , wherein at least one of the homogeneous catalyst compositions is a homogeneous transition metal catalyst.
13. The flexible manufacturing system for selectively producing different alpha-olefins according to claim 12 , wherein the homogeneous transition metal catalyst is prepared from a precursor metal selected from the group consisting of titanium, zirconium, chromium, nickel, tantalum, and tungsten.
14. The flexible manufacturing system for selectively producing different alpha-olefins according to claim 1 , wherein one or more of (an) organic ligand(s), (a) co-catalyst(s) and (a) modifier(s) is also provided to the reaction section.
15. The flexible manufacturing system for selectively producing different alpha-olefins according to claim 14 , wherein the co-catalyst is selected from the group consisting of organoaluminum compounds, inorganic borate salts, organic boron compounds, fluorinated aluminate salts, sodium hexafluoroantimonate, LiAlH 4 , and a mixture of magnesium and aluminum salts.
16. A method of sequentially producing different alpha-olefins from ethylene in the same manufacturing system comprising:
(a) providing a flexible manufacturing system including a reaction section with ethylene feed operative to oligomerize ethylene;
(ii) a catalyst feed system comprising a plurality of independent homogeneous catalyst feeders connected with the reaction section for alternatively providing different selective homogeneous catalyst compositions to the reaction section;
(iii) an ethylene recycle column coupled to the reaction section and adapted to receive crude product and unreacted ethylene therefrom, the recycle column being operative to separate ethylene and optionally lower oligomers from the crude product which are recycled to the ethylene feed to the reaction section, the ethylene recycle column being further operative to provide a crude product bottoms stream;
(iv) a catalyst removal section coupled to the reaction section adapted to remove spent catalyst from the system;
(v) a first product separation column connected to the recycle column receiving the crude product stream therefrom, the product separation column being operative to separate purified oligomer from the crude product stream; and optionally including
(vi) a second product separation column coupled to the first product separation column to receive bottoms therefrom and separate the bottoms from the first column into an overhead oligomerized product stream and a bottoms stream;
(b) operating the flexible manufacturing system with ethylene feed and a first homogeneous catalyst feed, wherein the first homogeneous catalyst is selective to a first alpha olefin composition;
(c) recovering the first alpha olefin composition; and thereafter
(d) operating the flexible manufacturing system with ethylene feed and a second homogeneous catalyst feed, wherein the second homogenous catalyst feed is selective to a second alpha olefin composition which is different from the first alpha olefin composition; and
(e) recovering the second alpha olefin composition.
17. The method of sequentially producing different alpha-olefins from ethylene in the same manufacturing system according to claim 16 , wherein the flexible manufacturing system for selectively producing different alpha-olefins is operated in step (b) or step (d) with a homogeneous catalyst composition comprising a titanate catalyst and organoaluminum cocatalyst selective for 1-butene, wherein selectivity to 1-butene is at least 85 weight % based on ethylene consumption.
18. The method of sequentially producing different alpha-olefins from ethylene in the same manufacturing system according to claim 16 , wherein the flexible manufacturing system for selectively producing different alpha-olefins is operated in step (b) or step (d) with a homogeneous catalyst composition comprising a chromium catalyst and an organoaluminum cocatalyst selective for 1-hexene, wherein selectivity to 1-hexene is at least 75 weight % based on ethylene consumption.
19. The method of sequentially producing different alpha-olefins from ethylene in the same manufacturing system according to claim 16 , wherein the flexible manufacturing system for selectively producing different alpha-olefins further comprises a second product separation column coupled to the first product separation column to receive bottoms therefrom and separate the bottoms from the first column into an overhead oligomeric product stream and a bottom stream and the system being operated with a homogeneous catalyst composition comprising a chromium catalyst, a phosphino amine cocatalyst, and an organoaluminum cocatalyst, the catalyst being selective for 1-octene and 1-hexene, wherein 1-hexene product is withdrawn as a product from the overhead of the first product separation column and 1-octene is withdrawn as overhead from the second product separation column and wherein selectivity to 1-octene is at least 65 weight % based on ethylene consumption and selectivity to 1-hexene and 1-octene collectively is at least 85 weight % based on ethylene consumption.
20. The method of sequentially producing different alpha-olefins from ethylene in the same manufacturing system according to claim 16 , comprising sequentially operating the flexible manufacturing system with ethylene feed and three different homogeneous catalysts to selectively produce three different alpha olefin product streams.