Process for producing C2 and C3 hydrocarbons

Patent metadata

Field	Value
Publication number	US-10287517-B2
Application number	US-201515538495-A
Country	US
Kind code	B2
Filing date	Dec 15, 2015
Priority date	Dec 22, 2014
Publication date	May 14, 2019
Grant date	May 14, 2019

Abstract

The invention relates to a process for producing C2 and C3 hydrocarbons, comprising a) subjecting a mixed hydrocarbon stream to first hydrocracking in the presence of a first hydrocracking catalyst to produce a first hydrocracking product stream; and b) subjecting the first hydrocarbon product stream to C4 hydrocracking optimized for converting C4 hydrocarbons into C3 hydrocarbons in the presence of a C4 hydrocracking catalyst to obtain a C4 hydrocracking product stream comprising C2 and C3 hydrocarbons.

First claim

The invention claimed is:

1. A process for producing C2 and C3 hydrocarbons, comprising
a) subjecting a mixed hydrocarbon stream to first hydrocracking in the presence of a first hydrocracking catalyst to produce a first hydrocracking product stream; and
b) subjecting the first hydrocarbon product stream to C4 hydrocracking optimized for converting C4 hydrocarbons into C3 hydrocarbons in the presence of a C4 hydrocracking catalyst to obtain a C4 hydrocracking product stream comprising C2 and C3 hydrocarbons, wherein steps (a) and (b) are performed in a single reactor having a first catalyst layer comprising the first hydrocracking catalyst and a last catalyst layer comprising the C4 hydrocracking catalyst.

2. The process according to claim 1 , wherein the first hydrocracking is a hydrocracking suitable for converting a hydrocarbon comprising naphthenic and paraffinic hydrocarbon compounds to a stream comprising at least 50 wt % LPG and 3-20 wt % aromatic hydrocarbons.

3. The process according to claim 1 , wherein the first hydrocracking catalyst is a catalyst containing one metal or two or more metals of group VIII, VI B or VII B of the periodic classification of elements deposited on a carrier.

4. The process according to claim 1 , wherein the C4 hydrocracking catalyst comprises a mordenite or an erionite.

5. The process according to claim 1 , wherein the C4 hydrocracking catalyst consists of a mordenite and an optional binder or comprises sulfided-nickel/H-Erionite1 and the C4 hydrocracking is performed under conditions comprising a temperature between 325 and 450° C., a partial hydrogen pressure between 2 and 4 MPa, a molar ratio hydrogen to hydrocarbon feed of 2:1 to 8:1, wherein the number of moles of the hydrocarbon feed is based on the average molecular weight of the hydrocarbon feed and a VVH of 0.5 to 5 h −1 .

6. The process according to claim 1 , wherein the C4 hydrocracking is performed without compressing or expanding the first hydrocracking product stream.

7. The process according to claim 1 , wherein the temperature for the C4 hydrocracking is higher than the temperature for the first hydrocracking.

8. The process according to claim 1 , wherein the mixed hydrocarbon feedstream comprises naphtha, gasoline, coke oven light oil, reformate, or mixtures thereof.

9. The process according to claim 1 , further comprising the step of
c) separating the C4 hydrocracking product stream to provide at least a light hydrocarbon stream comprising at least C2 and C3 hydrocarbons, a middle hydrocarbon stream comprising C4 and/or C5 hydrocarbons and a heavy hydrocarbon stream comprising at least C6+ hydrocarbons.

10. The process according to claim 9 , further comprising the step of
d) subjecting the heavy hydrocarbon stream to second hydrocracking in the presence of a second hydrocracking catalyst to produce a second hydrocracking product stream comprising BTX, wherein the second hydrocracking is more severe than the first hydrocracking.

11. The process according to claim 9 , wherein at least part of C5 hydrocarbon in the middle hydrocarbon stream is recycled back to the first hydrocracking of step a).

12. The process according to claim 1 , wherein the amount of methane in the first hydrocracking product stream is at most 5 wt %.

13. The process according to claim 1 , wherein the amount of the C2-C3 hydrocarbons in the C4 hydrocracking product stream is at least 60 wt %.

14. The process according to claim 8 , wherein the mixed hydrocarbon feedstream has a boiling point range of 20−200° C.

15. A process for producing C2 and C3 hydrocarbons, comprising
a) subjecting a mixed hydrocarbon stream to first hydrocracking in the presence of a first hydrocracking catalyst to produce a first hydrocracking product stream; and
b) subjecting the first hydrocarbon product stream to C4 hydrocracking optimized for converting C4 hydrocarbons into C3 hydrocarbons in the presence of a C4 hydrocracking catalyst to obtain a C4 hydrocracking product stream comprising C2 and C3 hydrocarbons, wherein steps (a) and (b) are performed in a single reactor comprising a layer comprising both the first hydrocracking catalyst and the C4 hydrocracking catalyst, wherein the proportion of the C4 hydrocracking catalyst at the end of the bed is higher than the proportion of the C4 hydrocracking catalyst at the beginning of the bed.

16. The process according to claim 15 , wherein the first hydrocracking catalyst is a catalyst containing one metal or two or more metals of group VIII, VI B or VII B of the periodic classification of elements deposited on a carrier.

17. The process according to claim 15 , wherein the C4 hydrocracking catalyst comprises a mordenite or an erionite.

18. The process according to claim 15 , wherein the C4 hydrocracking is performed without compressing or expanding the first hydrocracking product stream.

19. The process according to claim 15 , wherein the temperature for the C4 hydrocracking is higher than the temperature for the first hydrocracking.

20. The process according to claim 15 , further comprising the step of
d) subjecting the heavy hydrocarbon stream to second hydrocracking in the presence of a second hydrocracking catalyst to produce a second hydrocracking product stream comprising BTX, wherein the second hydrocracking is more severe than the first hydrocracking, wherein at least part of C5 hydrocarbon in the middle hydrocarbon stream is recycled back to the first hydrocracking of step a).

Assignees

• Sabic Global Technologies Bv

Inventors

• Oprins Arno Johannes Maria
• Davies Andrew P
• Ward Andrew Mark
• Wong Kae Shin
• Aramburo Luis
• Van Iersel Maikel

Classifications

• C10G2400/26

  Fuel gas · CPC title

• C10G65/18 Primary

  including only cracking steps · CPC title

• C10G65/10

  including only cracking steps · CPC title

• C10G2300/1048

  Middle distillates · CPC title

• C10G2400/28

  Propane and butane · CPC title