Process for inhibiting oligomerization of C3- to C5-olefins
Oligomerization of C 3 - to C 5 -olefins using a catalyst is inhibited, wherein the oligomerization is carried out in at least one reaction stage including at least one reactor and at least one distillation column, and wherein the oligomer content in the feed stream to the at least one reactor of the at least one reaction stage is at least 1% by weight.
1. A process for the specific inhibition of oligomerization of C 3 - to C 5 -olefins, comprising:
oligomerizing a feed mixture comprising the C 3 - to C 5 -olefins in the presence of a heterogeneous oligomerization catalyst in at least one reaction stage, the at least one reaction stage in each case comprising:
at least one reactor in which the oligomerization of the C 3 - to C 5 -olefins is carried out to form an oligomerizate, and
at least one distillation column in which the oligomers formed in the oligomerization are at least partially separated from a residual oligomerizate,
wherein the oligomerization is inhibited by the fact that a content of oligomers in the feed to the at least one reactor of the at least one reaction stage, which comprises recycled residual oligomerizate and a fresh feed of the feed mixture, is at least 1% by weight, based on a total composition of the feed,
with the proviso that the inhibition is carried out only when a predetermined value of a process or plant parameter is exceeded, which indicates that the reaction rate of the oligomerization exceeds threshold, at least locally, in one or more reactors, based on the respective reactor.
2. The process according to claim 1 , wherein the content of oligomers in the feed to at least one reactor of the at least one reaction stage is 1% by weight to 10% by weight, based on the total composition of the feed.
3. The process according to claim 1 , wherein the heterogeneous oligomerization catalyst is a transition metal-containing oligomerization catalyst comprising:
a transition metal compound, and
a support material.
4. The process according to claim 3 , wherein the heterogeneous oligomerization catalyst has a composition of:
15 to 40% by weight NiO,
5 to 30% by weight Al 2 O 3 ,
55 to 80% by weight SiO 2 , and
0.01 to 2.5% by weight of an alkali metal oxide.
5. The process according to claim 3 , wherein the support material s aluminosilicate support material.
6. The process according to claim 1 , wherein the oligomerization in each of the reaction stages present is carried out at a temperature in a range of 50 to 200° C.
7. The process according to claim 6 , wherein the temperature is in the range of 60 to 130° C.
8. The process according to claim 1 , wherein a pressure in the oligomerization in each of the reaction stages present is from 10 to 70 bar.
9. The process according to claim 8 , wherein the pressure is from 20 to 55 bar.
10. The process according to claim 1 , wherein C 4 -olefins are used in process.
11. The process according to claim 1 , wherein the process or plant parameter, which indicates that the reaction rate exceeds threshold, is a temperature increase, an absolute or local temperature in the reactor, a concentration of products and/or by-products, a pressure increase due to an increasing vapour pressure at elevated temperature, and/or a pressure loss across the reactor.
12. A process for oligomerization of C 3 - to C 5 -olefins, comprising:
oligomerizing a feed mixture comprising C 3 - to C 5 -olefins in the presence of an oligomerization catalyst in at least one reaction stage to obtain an oligomerizate,
separating the oligomers formed at least partially in at least one downstream distillation column from a residual oligomerizate, wherein the residual oligomerizate is at least partially recycled to the at least one reactor,
wherein the reaction stage or at least one of the reaction stages comprises at least one adiabatically operated reactor,
wherein, in the adiabatically operated reactor, a temperature increase, the difference between the temperature of the reactor discharge and the temperature of the reactor feed, is at least temporarily 40 K or more, and
monitoring the temperature increase, and
when the temperature increase exceeds a threshold value of 40 K, the oligomer content in the feed to the at least one reactor of the at least one reaction stage, which comprises recycled residual oligomerizate and a fresh feed of the feed mixture, is adjusted to 1% by weight to 10% by weight, based on a total composition of the feed.
13. The process according to claim 12 , wherein the heterogeneous oligomerization catalyst is a transition metal-containing oligomerization catalyst comprising
a transition metal compound, and
a support material.
14. The process according to claim 13 , wherein the heterogeneous oligomerization catalyst has a composition of
15 to 40% by weight NiO,
5 to 30% by weight Al 2 O 3 ,
55 to 80% by weight SiO 2 , and
0.01 to 2.5% by weight of an alkali metal oxide.
15. The process according to claim 13 , wherein the support material aluminosilicate support material.
16. The process according to claim 12 , wherein the oligomerization in each of the reaction stages present is carried out at a temperature in a range of 50 to 200° C.
17. The process according to claim 16 , wherein the temperature is in the range of 60 to 130° C.
18. The process according to claim 12 , wherein a pressure in the oligomerization in each of the reaction stages present is from 10 to 70 bar.
19. The process according to claim 18 , wherein the pressure is from 20 to 55 bar.
20. The process according to claim 12 , wherein C 4 -olefins are used in the process.