Adsorbent materials and methods of use

Patent metadata

Field	Value
Publication number	US-2016175759-A1
Application number	US-201514963371-A
Country	US
Kind code	A1
Filing date	Dec 9, 2015
Priority date	Dec 23, 2014
Publication date	Jun 23, 2016
Grant date	—

Abstract

Adsorbent materials comprising a core, for example CHA, and at least one coating, for example DDR, are provided herein. Adsorbent contactors and gas separation processes using the adsorbent materials are also provided herein.

First claim

What is claimed is:

1 . An adsorbent material comprising
a porous, solid core, wherein the core has a volume adsorptive capacity of less than 35% of the volume of the adsorbent material and at least one coating on the core, wherein the at least one coating has a kinetic selectivity for CO 2 over CH 4 of greater than 10.

2 . The adsorbent material of claim 1 , wherein the core comprises a zeolite.

3 . The adsorbent material of claim 2 , wherein the zeolite comprises chabasite (CHA).

4 . The adsorbent material of claim 3 , wherein CHA is selected from the group consisting of Si-CHA, SAPO-34, AlPO-34, SSZ-13 and a combination thereof.

5 . The adsorbent material of claim 1 , wherein the at least one coating comprises a zeolite.

6 . The adsorbent material of claim 5 , wherein the zeolite comprises DDR.

7 . The adsorbent material of claim 6 , wherein DDR is selected from the group consisting of Sigma-1, ZSM-58 and a combination thereof.

8 . The adsorbent material of claim 1 , wherein the core comprises Si-CHA and the at least one coating comprises Sigma-1.

9 . The adsorbent material of claim 1 , wherein the at least one coating and the core are present in a weight ratio of coating to core of about 6:1 to about 30:1.

10 . The adsorbent material of claim 1 , wherein the at least one coating and the core are present in a weight ratio of coating to core of about 1:1.

11 . The adsorbent material of claim 1 , wherein the adsorbent material is in the form of particles having an average particle size from about 2 μm to about 20 μm.

12 . An adsorbent material comprising
a core comprising CHA and at least one coating on the core, wherein the coating comprises DDR.

13 . The adsorbent material of claim 12 , wherein the core has a volume adsorptive capacity of less than 35% of the volume of the adsorbent material.

14 . The adsorbent material of claim 12 , wherein the at least one coating has a kinetic selectivity for CO 2 over CH 4 of greater than 50.

15 . The adsorbent material of claim 12 , wherein CHA is Si-CHA and DDR is Sigma-1.

16 . The absorbent material of claim 1 , wherein the core is CHA and the coating is Sigma-1.

17 . The absorbent material of claim 1 , wherein the core is CHA and the coating is SiO 2 silica.

18 . The absorbent material of claim 1 , wherein the core is ZSM-58 and the coating is Sigma-1.

19 . The absorbent material of claim 1 , wherein the core is CHA and the coating is ZSM-58.

20 . The absorbent material of claim 1 , wherein the core is ZSM-5 and the coating is UZM-19.

21 . The absorbent material of claim 1 , wherein the core is CHA and the coating is AEI.

22 . The absorbent material of claim 1 , wherein the core is DDR and the coating is DOH.

23 . An adsorbent contactor for use in swing adsorption gas separation process units, comprising: a) a gas inlet end; and b) a gas outlet end; wherein the gas inlet end and the gas outlet end are in fluid connection by a plurality of open flow channels wherein the surface of the open flow channels are comprised of the adsorbent material of claim 1 .

24 . A gas separation process comprising contacting a gas mixture containing at least one contaminant with an adsorbent material of claim 1 .

25 . The process of claim 24 , wherein the gas mixture comprises CH 4 and the at least one contaminant is CO 2 , N 2 , H 2 O, H 2 S, NO x and SO x .

26 . The process of claim 24 , wherein the gas mixture comprises olefinic and paraffinic gas and the at least one contaminant is the olefinic gas.

27 . The process of claim 24 , wherein the process comprises PSA, TSA, PPSA, PTSA, RCPSA, RCTSA, RC-PPSA or RC-PTSA.

28 . A process for selectively separating CO 2 from a feed gas mixture, the process comprising:
a) contacting the feed gas mixture under sorption conditions with the adsorbent material of claim 1 ; b) sorbing the CO 2 into/onto the sorbent; c) subjecting the sorbent to desorption conditions by which at least a portion of the sorbed CO 2 is desorbed; and d) retrieving a CO 2 -rich product stream that has a higher mol % of CO 2 than the feed gas mixture.

29 . The process of claim 28 , wherein the feed gas mixture comprises CH 4 .

30 . The adsorbent material of claim 1 , wherein the at least one coating has a diffusion coefficient for CO 2 of greater than 1.0 e-13 under ambient conditions.

31 . The adsorbent material of claim 30 , wherein the at least one coating has a diffusion coefficient for CO 2 of greater than 1.0 e-11 under ambient conditions.

Assignees

• Carstensen Barbara
• Leta Daniel P
• Kamakoti Preeti
• Ravikovitch Peter
• Varon Joshua
• Beutel Tilman Wolfram
• Strohmaier Karl Gottlieb
• Johnson Ivy Dawn
• Deckman Harry W
• Wang Frank Cheng-Yu
• Paur Charanjit Singh
• Exxonmobil Res & Eng Co

Inventors

• Carstensen Barbara
• Leta Daniel P
• Kamakoti Preeti
• Ravikovitch Peter
• Varon Joshua
• Beutel Tilman Wolfram
• Strohmaier Karl Gottlieb
• Johnson Ivy Dawn
• Deckman Harry W
• Wang Frank Cheng-Yu
• Paur Charanjit Singh

Classifications

• B01D2253/108

  Zeolites · CPC title

• B01D2253/106

  Silica or silicates · CPC title

• B01J20/28004

  Sorbent size or size distribution, e.g. particle size · CPC title

• B01J20/18

  Synthetic zeolitic molecular sieves · CPC title

• B01D53/02 Primary

  by adsorption, e.g. preparative gas chromatography {(solid sorbent compositions B01J20/00, preparation of inorganic compounds or elements C01)} · CPC title