Use of molten salt to separate carbon from a molten metal catalyst

Patent metadata

Field	Value
Publication number	US-12168606-B2
Application number	US-202017428301-A
Country	US
Kind code	B2
Filing date	Feb 5, 2020
Priority date	Feb 5, 2019
Publication date	Dec 17, 2024
Grant date	Dec 17, 2024

Abstract

The present invention relates to a method for molten metal pyrolysis of hydrocarbons to produce hydrogen gas and carbon. Liquid salt is used to separate produced carbon from the molten metal and to facilitate isolation of produced carbon.

First claim

The invention claimed is:

1. Method for producing solid carbon and hydrogen gas by molten metal pyrolysis of hydrocarbons, the method comprising:
(i) feeding a stream of hydrocarbon into a pyrolysis reactor through a catalytic layer of molten metal to pyrolise the hydrocarbon into solid carbon and hydrogen gas;
(ii) feeding a stream of molten salt into the pyrolysis reactor to separate the solid carbon from the molten metal
(iii) collecting a product gas containing hydrogen gas that evolves from the reactor;
(iv) collecting a mixture comprising solid carbon and molten salt;
(v) separating the mixture obtained in step (iv) into a product comprising solid carbon and separated salt
wherein the separation step (v) involves separating solid carbon from the separated salt by filtering and/or washing the mixture with an aqueous liquid to obtain a product comprising pure solid carbon and a separated salt, and wherein the separated salt is recycled into the reactor as part of step (ii).

2. The method according to claim 1 , wherein the metal in the molten metal is selected from the group consisting of In, Bi, Sn, Ga, Pb, Ag, Cu, Pt, Ni, and Au.

3. The method according to claim 1 , wherein the salt has a heat capacity of at most 2 J/K, and/or wherein the salt comprises at least one of KNO3, NaNO3, NaCl, KCl, LiCl, MgCl2, CuCl, NiCl2, ZnCl2, ZnBr2 and NaBr.

4. The method according to claim 1 , wherein the hydrocarbon comprises a C1-C4 hydrocarbon.

5. The method according to claim 1 , further comprising:
(vi) separating the product gas obtained in step (iii) into unconverted hydrocarbon gas and hydrogen gas, to obtain purified hydrogen gas and recovered hydrocarbon.

6. The method according to claim 5 , wherein the recovered hydrocarbon is recycled back into the pyrolysis reactor as part of step (i).

7. The method according to claim 1 , wherein the reactor has an inlet for receiving the hydrocarbon at or near the bottom end of the reactor, an outlet for discharging a mixture of carbon and molten salts in a side wall, and an outlet for discharging a product gas comprising hydrogen at or near the top end.

8. The method according to claim 1 , wherein a layer of molten salt is present in the pyrolysis reactor, and wherein step (iv) involves skimming to collect the solid carbon and part the layer of molten salt, such that substantially all of the solid carbon is removed from the reactor.

9. The method according to claim 1 , wherein separating solid carbon from the separated salt by filtering is done by using a metal filter or a ceramic filter.

10. The method according to claim 1 , wherein the reactor is kept at a temperature in the range of 250-1500° C.

11. The method according to claim 4 , wherein the hydrocarbon is methane.

12. The method according to claim 5 , wherein separating the product gas obtained in step (iii) into unconverted hydrocarbon gas and hydrogen gas is done by using an adsorbent material.

Assignees

• TNO

Inventors

• Goetheer Earl Lawrence Vincent
• Bhardwaj Rajat
• Roelands Cornelis Petrus Marcus
• Linders Marco Johannes Gerardus

Classifications

• B01J35/27

  in a liquid or molten state · CPC title

• B01D71/0223

  Group 8, 9 or 10 metals · CPC title

• C01B2203/148

  involving a recycle stream to the feed of the process for making hydrogen or synthesis gas · CPC title

• C01B2203/1241

  Natural gas or methane · CPC title

• C01B2203/085

  by electric heating · CPC title