Covalent-Organic Framework Materials and Methods of Making Thereof

Patent metadata

Field	Value
Publication number	US-2022323935-A1
Application number	US-202017641055-A
Country	US
Kind code	A1
Filing date	Sep 15, 2020
Priority date	Sep 16, 2019
Publication date	Oct 13, 2022
Grant date	—

Abstract

The present invention provides a covalent-organic framework (COF) body, populations of such bodies, a method for manufacturing a covalent-organic framework (COF) body, and (a) a gas storage system or a gas separation system comprising a gas storage vessel and a population of such COF bodies. The COF body comprises a plurality of primary COF particles, some or all of the primary COF particles being agglomerated as COF agglomerates. The average diameter of the primary COF particles is between nm and 120 nm, and the average diameter of the agglomerates is larger than the average diameter of the primary COF particles and between 15 nm and 250 nm. By careful control over particle size distribution during the formation of the COF material, it is possible (b) to form COF materials into high bulk density shapes and forms which are industrially useful and practical without losing sorbent performance.

First claim

1 . A covalent-organic framework (COF) body comprising a plurality of primary COF particles, some or all of the primary COF particles being agglomerated as COF agglomerates, wherein:
the average diameter of the primary COF particles is between 10 nm and 120 nm; the average diameter of the agglomerates is larger than the average diameter of the primary COF particles and between 15 nm and 250 nm.

2 . (canceled)

3 . The covalent-organic framework (COF) body according to claim 1 wherein not more than 10% of the agglomerates forming part of the covalent-organic framework (COF) body have a diameter greater than 800 nm.

4 . The covalent-organic framework (COF) body according to claim 1 wherein the COF agglomerates and/or primary COF particles forming the body are formed from a single COF composition.

5 . The covalent-organic framework (COF) body according to claim 1 wherein the COF agglomerates and/or primary COF particles forming the body are formed from two or more different COF compositions.

6 . The covalent-organic framework (COF) body according to claim 1 wherein COF agglomerates and/or primary COF particles forming the body comprise an imine and/or a hydrazone linked COF composition.

7 . The covalent-organic framework (COF) body according to claim 1 wherein the bulk density of the body is at least 80% of the calculated density of a COF single crystal of the same composition as the body.

8 . The covalent-organic framework (COF) body according to claim 1 wherein the volume of the body is at least 0.5 mm 3 .

9 . A method for manufacturing a covalent-organic framework (COF) body, comprising the steps of: providing a COF material comprising primary COF particles and agglomerates of primary COF particles, the primary COF particles having an average diameter of between 10 nm and 120 nm, the agglomerates having an average diameter of between 15 nm and 250 nm;
centrifuging a liquid suspension comprising the COF material and one or more selected solvents to form a COF concentrate; and performing a temperature-controlled drying step to remove at least some of the solvent from the COF concentrate to thereby form the COF body.

10 . The method according to claim 9 wherein the step of providing a COF material comprising primary COF particles and agglomerates of primary COF particles includes allowing the reaction of COF precursors in a reaction mix including one or more selected solvents to thereby form the particles and/or particle agglomerates of the COF material.

11 . The method according to claim 10 wherein the reaction mix further comprises one or more catalysts selected from one or more of: a metal triflate; p-toluenesulfonic acid; acetic acid; benzoic acid; p-nitrobenzenesulfonic acid; benzenesulfonic acid; p-phenolsulfonic acid; trifluoroacetic acid; hydrochloroic acid; and/or sulphuric acid.

12 . The method according to claim 9 wherein the one or more solvents are selected from one or more of mesitylene, 1,4-dioxane, acetonitrile, methanol, ethanol, isopropanol, n-butanol, 1,2-dichlorobenzene, 1-chlorobenzene, water, acetone, N,N-dimethylformamide, N-methyl-2-pyrrolidone, aniline, m-cresol, dimethylsulfoxide, tetrahydrofuran, toluene, chloroform, dichoromethane, xylene, tetrachloroethane, and/or trichloroethane.

13 . The method according to claim 12 wherein the one or more solvents comprise acetonitrile (CH 3 CN) in combination with a 1:1 (v/v) mixture of mesitylene and 1,4-dioxane.

14 . The method according to claim 12 wherein the one or more solvents comprise acetone in combination with 1,4-dioxane.

15 . (canceled)

16 . The method according to claim 9 wherein the density of the one or more solvents is selected to be less than the calculated density of a single crystal of the COF material.

17 . The method according to claim 9 wherein the absolute density difference between the one or more solvents and the calculated density of a single crystal of the COF material is >0.2 g/l.

18 . The method according to claim 9 wherein the temperature-controlled drying step is performed with a maximum temperature of not more than 60° C.

19 . (canceled)

20 . The method according to claim 9 wherein the method includes a step of activating the COF material by washing the COF material in a suitable solvent.

21 . The method according to claim 20 wherein the COF material is activated by washing the COF material in supercritical carbon dioxide.

22 . The method according to claim 21 wherein the temperature-controlled drying step is performed after the step of washing the COF material in supercritical carbon dioxide, and wherein the temperature-controlled drying step is performed at a pressure release rate of from about 0.1 bar/h to about 20 bar/h.

23 .- 24 . (canceled)

25 . A gas storage system or a gas separation system comprising a gas storage vessel and a population of COF bodies according to claim 1 , wherein the population of COF bodies is disposed within the gas storage vessel.

Assignees

• Cambridge Entpr Ltd

Inventors

• Fairen-Jimenez David
• Carrington Mark Egdell

Classifications

• B01J20/3028

  Granulating, agglomerating or aggregating · CPC title

• B01J20/28011

  Other properties, e.g. density, crush strength · CPC title

• B01J20/28069

  Pore volume, e.g. total pore volume, mesopore volume, micropore volume · CPC title

• B01J20/3085

  Chemical treatments not covered by groups B01J20/3007 - B01J20/3078 · CPC title

• B01D53/02

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