Process for the conversion of oxygenates to olefins

Patent metadata

Field	Value
Publication number	US-2016296923-A1
Application number	US-201615183506-A
Country	US
Kind code	A1
Filing date	Jun 15, 2016
Priority date	Jun 29, 2012
Publication date	Oct 13, 2016
Grant date	—

Abstract

The present invention relates to a process for converting oxygenates to olefins, comprising
(1) providing a gas stream comprising one or more ethers; (2) contacting the gas stream provided in (1) with a catalyst,

the catalyst comprising
a support substrate and a layer applied to the substrate,

the layer comprising one or more zeolites of the MFI, MEL and/or MWW structure type.

First claim

1 - 27 . (canceled)

28 . A process for converting oxygenates to olefins, the process comprising:
providing a gas stream comprising one or more ethers; contacting a catalyst, which includes a support substrate and a catalytic layer applied to the substrate, the layer comprising one or more zeolites of the MFI, MEL, or MWW structure type or any one mixture thereof, with the gas stream.

29 . The process according to claim 27 , wherein the support substrate is selected from the group consisting of granules, pellets, meshes, rings, spheres, cylinders, hollow cylinders, monoliths and mixtures thereof, and any one combination of two or more thereof.

30 . The process according to claim 27 , wherein the one or more monoliths are selected from the group consisting of honeycombs, braids, foams and combinations of two or more thereof.

31 . The process according to claim 27 , wherein the support substrate is selected from a ceramic substrate, metallic substrate, or mixed a ceramic/metallic substrate.

32 . The process according to claim 27 , wherein the one or more zeolites includes the MFI structure type.

33 . The process according to claim 27 , wherein the catalyst comprises the one or more zeolites includes a total loading of 0.005 to 1 g/cm 3 based on the volume of the coated support substrate.

34 . The process according to claim 27 , wherein the one or more ethers are selected from di(C 1 -C 3 )alkyl ethers, and the ethers are present in a range from 30% to 100% by volume, based on the total volume of the gas stream.

35 . The process according to claim 34 , wherein one or more ethers in the gas stream is obtained from the dehydration of one or more aliphatic alcohols.

36 . The process according to claim 27 , wherein water is present in the gas stream in a range from 5 to 60% by volume, based on the total volume of the gas stream.

37 . The process according to claim 34 , wherein the contacting of the catalyst with the gas stream is conducted at a temperature in range from 200° to 700° C., and at a pressure in a range from 0.1 to 10 bar.

38 . The process according to claim 37 , wherein the contacting of the catalyst with the gas stream is a continuous process with a space velocity in a range from 0.5 to 50 h −1 .

39 . The process according to claim 38 , wherein the catalyst has a service life without interruption in a range from 15 to 200 h.

40 . The process according to claim 38 , further comprising calcining the catalyst to provide a regenerated catalyst, providing the gas stream, and contacting the regenerated catalyst with the gas stream.

41 . The process according to claim 40 , wherein the calcination is performed at a temperature in a range from 200° to 1100° C.

42 . The process according to claim 41 , wherein the calcination is performed for a period of 025 to 30 h.

43 . The process according to claim 40 , wherein the catalyst can be regenerated from 10 to 1000 times following each process cycle.

44 . The process according to claim 27 , wherein the catalyst is prepared by a process comprising
(i) providing the support substrate and the one or more zeolites of the MFI, MEL, or MWW structure type, or any one mixture thereof; (ii) preparing a mixture comprising the one or more zeolites and one or more solvents; (iii) homogenizing the mixture obtained in step (ii); (iv) coating the support substrate with the homogenized mixture obtained in step (iii); (v) optionally drying the coated support substrate obtained in step (iv); and (vi) optionally calcining the coated support substrate obtained in step (iv) or step (v).

45 . The process according to claim 44 , wherein the drying in step (v) is conducted at a temperature in a range from 50° to 220° C., or the the calcining in step (vi) is conducted at a temperature in a range from 300° to 850° C.

46 . The process according to claim 44 , wherein the one or more solvents are selected from the group consisting of alcohols, water, mixtures of two or more alcohols, and mixtures of water and one or more alcohols.

47 . The process according to claim 44 , wherein the mixture prepared in step (ii) includes a solids concentration in a range from 10% to 75% by weight.

48 . The process according to claim 44 , wherein the homogenizing in step (iii) is conducted by stirring, kneading, agitating, vibrating or any one combination thereof, and the coating in step (iv) is conducted by spray coating, wash coating or a combination of the two.

49 . The process according to claim 44 , wherein the step (iv) is repeated once or more than once.

Assignees

• Basf Se

Inventors

• Spannhoff Kirsten
• Patcas Florina Corina
• Schwab Ekkehard
• Weck Alexander
• Bay Kerem

Classifications

• B01J29/40 Primary

  of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively · CPC title

• C07C1/20

  starting from organic compounds containing only oxygen atoms as heteroatoms · CPC title

• C07C2523/78

  with alkali- or alkaline earth metals or beryllium · CPC title

• B01J37/08

  Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title

• B01J37/0236

  Drying, e.g. preparing a suspension, adding a soluble salt and drying · CPC title