Process for catalytic cracking of naphtha using radial flow moving bed reactor system

Patent metadata

Field	Value
Publication number	US-11208599-B2
Application number	US-201816604235-A
Country	US
Kind code	B2
Filing date	Mar 13, 2018
Priority date	May 10, 2017
Publication date	Dec 28, 2021
Grant date	Dec 28, 2021

Abstract

A method of catalytically cracking liquid hydrocarbons is disclosed. The method includes the use of one or more radial flow moving bed reactors. The method may include mixing a liquid hydrocarbon stream comprising primarily C5 and C6 hydrocarbons with water or a dry gas to form a feed mixture and flowing the feed mixture into the one or more radial flow moving bed reactors in a manner so that the feed mixture flows radially inward or radially outward through the moving catalyst bed and thereby contacts the catalyst particles under reaction conditions to produce a hydrocarbon stream comprising light olefins (C2 to C4 olefins).

First claim

The invention claimed is:

1. A method of catalytically cracking liquid hydrocarbons, the method comprising: adding catalyst particles to a catalyst entry location of a radial flow moving bed reactor; allowing the catalyst particles to move by gravity through the radial flow moving bed reactor to an exit location of the radial flow moving bed reactor, wherein the catalyst particles form a moving catalyst bed in the radial flow moving bed reactor; mixing a liquid hydrocarbon stream comprising C 5 and C 6 hydrocarbons with water or a dry gas to form a feed mixture; flowing the feed mixture into the radial flow moving bed reactor in a manner so that the feed mixture flows radially inward or radially outward through the moving catalyst bed and thereby contact the catalyst particles under reaction conditions to produce a hydrocarbon stream comprising light olefins wherein the light olefins comprise C 2 to C 4 olefins; and flowing the hydrocarbon stream comprising light olefins greater than 50 wt. % C 2 and C 3 hydrocarbons from the radial flow moving bed reactor.

2. The method of claim 1 , further comprising:
flowing spent catalyst from the radial flow moving bed reactor to a catalyst regenerator;
regenerating the spent catalyst in the catalyst regenerator; and
flowing regenerated catalyst from the catalyst regenerator to the radial flow moving bed reactor via the catalyst entry location.

3. The method of claim 1 , wherein the dry gas comprises hydrogen.

4. The method of claim 1 , wherein flowing of the feed mixture is radially outward.

5. The method of claim 1 , wherein the liquid hydrocarbon stream has a boiling end point of less than 350° C.

6. The method of claim 1 , wherein the reaction conditions comprise a weight hourly space velocity (WHSV) in a range 1 to 15 hr −1 .

7. The method of claim 1 , wherein the reaction conditions comprise a reaction temperature in a range 450 to 900° C.

8. The method of claim 1 , wherein the catalyst particles comprise pure ZSM-5 treated with phosphorous.

9. The method of claim 1 , wherein the liquid hydrocarbon stream comprises a selection from the list consisting of: light naphtha, heavy naphtha, kerosene, diesel, and combinations thereof.

10. The method of claim 1 , further comprising:
recycling uncracked C 5 and C 6 hydrocarbons back to the radial flow moving bed reactor.

11. The method of claim 1 , wherein water/liquid hydrocarbon stream volumetric ratio is in the range 0 to 10.

12. A method of catalytically cracking liquid hydrocarbons, the method comprising: processing a feed stream comprising paraffinic C 5 and C 6 hydrocarbons mixed in a series of radial flow moving bed reactors, wherein processing in a first radial flow moving bed reactor in the series of radial flow moving bed reactors comprises:
adding catalyst particles to a catalyst entry location of the first radial flow moving bed reactor;
allowing the catalyst particles to move by gravity through the first radial flow moving bed reactor to an exit location of the first radial flow moving bed reactor, wherein the catalyst particles form a first moving catalyst bed in the first radial flow moving bed reactor;
mixing the feed stream with water or dry gas to form a feed mixture;
flowing the feed mixture into the first radial flow moving bed reactor in a manner so that the feed mixture flows radially inward or radially outward through the first moving catalyst bed and thereby contact the catalyst particles under reaction conditions to produce a first hydrocarbon effluent stream comprising greater than 50 wt. % light olefins, wherein the light olefins comprise C 2 to C 4 olefins;
flowing the first hydrocarbon effluent stream into a second radial flow moving bed reactor of the series of radial flow moving bed reactors for further processing;
flowing spent catalyst from the series of radial flow moving bed reactors to a catalyst regenerator;
regenerating the spent catalyst in the catalyst regenerator; and
flowing regenerated catalyst from the catalyst regenerator to the series of radial flow moving bed reactors.

13. The method of claim 12 , wherein the catalyst particles comprise pure ZSM-5 treated with phosphorous.

14. The method of claim 12 , wherein each reactor in the series of radial flow moving bed reactors, other than the first radial flow moving bed reactor in the series, receives an effluent stream from the prior reactor in the series and processes an effluent stream from the prior reactor in the series to produce an effluent stream comprising more light olefins than the effluent stream from the prior reactor in the series.

15. The method of claim 12 , wherein radial flow moving bed reactors in series after the first radial flow moving bed reactor (subsequent reactors) is adapted to operate so that influent for each of the subsequent reactors flows radially inward or radially outward through the each of the subsequent reactors and thereby contact the catalyst particles under reaction conditions to produce a hydrocarbon effluent stream comprising more light olefins than the effluent stream from the prior reactor in the series.

16. The method of claim 12 , wherein the dry gas is a selection from the list consisting of: methane (CH 4 ), hydrogen (H 2 ), and combinations thereof.

17. The method of claim 12 , wherein flowing the feed mixture radially outward causes the flow of the feed mixture to be perpendicular or substantially perpendicular to movement of the catalyst bed.

18. The method of claim 12 , wherein the feed stream comprises a liquid hydrocarbon stream that has an end point of less than 350° C. and at least one of the reactors in the series operate under reaction conditions that comprise a selection from the list consisting of: (1) a weight hourly space velocity (WHSV) in a range from 1 to 15 hr −1 , (2) a reaction temperature in a range 450 to 900° C., (3) a pressure in a range of vacuum to 10 bars.

19. The method of claim 18 , wherein the feed stream comprises a selection from the list consisting of: light naphtha, heavy naphtha, kerosene, diesel, and combinations thereof.

20. A method of catalytically cracking liquid hydrocarbons, the method comprising: processing a feed stream comprising paraffinic C 5 and C 6 hydrocarbons mixed in a series of radial flow moving bed reactors, wherein processing in a first radial flow moving bed reactor in the series of radial flow moving bed reactors comprises:
adding catalyst particles to a catalyst entry location of the first radial flow moving bed reactor;
allowing the catalyst particles to move by gravity through the first radial flow moving bed reactor to an exit location of the first radial flow moving bed reactor, wherein the catalyst particles form a first moving catalyst bed in the first radial flow moving bed reactor;
mixing the feed stream with water or dry gas to form a feed mixture;
flowing the feed mixture into the first radial flow moving bed reactor in a manner so that the feed mixture flows radially inward or radially outward through the first moving catalyst bed and thereby contact the catalyst particles under reaction conditions to produce a first hydrocarbon effluent stream comprising light olefins, wherein the light olefins comprise C 2 to C 4 olefins;
flowing the first hydrocarbon effluent stream into a second radial flow moving bed reactor of the series of radial flow moving bed reactors for further processing;
flowing spent catalyst from the series of radial flow moving bed reactors to a catalyst regenerator;
regenerating t

Assignees

• Sabic Global Technologies Bv

Inventors

• Alarifi Abdulaziz S
• Al-Majnouni Khalid A
• Al-Zenaidi Ahmed

Classifications

• C10G11/16 Primary

  according to the "moving bed" method · CPC title

• C10G2300/4006

  Temperature · CPC title

• C10G2300/4018

  Spatial velocity, e.g. LHSV, WHSV · CPC title

• C10G2300/1048

  Middle distillates · CPC title

• C10G2300/1055

  Diesel having a boiling range of about 230 - 330 °C · CPC title