IP Library › Granted Patent US 12,599,885
Granted Patent B2
US 12,599,885 · App. 17/906,108 · Granted Apr 14, 2026

Methods of pneumatic carbon removal

Inventors: Samuel Shaner (Goleta, CA); Zachary Jones (Goleta, CA); Andrew Caldwell (Goleta, CA); Fadl Saadi (Goleta, CA)
Assignee: MOLTEN INDUSTRIES INC.
B01J10/005B01J6/008B01J8/0055B01J8/006B01J8/007B01J8/224C01B32/05
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Quick Facts
Patent No.
US 12,599,885
App. No.
17/906,108
Granted
Apr 14, 2026
Kind
B2
Abstract

A pyrolysis process comprises introducing one or more chemical reactants into a reactor containing a liquid maintained at a high temperature, producing chemical products in the liquid based on the high temperature, allowing the solid product to grow in particle size, accumulating the solid product in the liquid, and removing the solid product from the reactor while retaining a substantial portion of the liquid within the reactor. The chemical products comprise a solid chemical product that is mixed with the liquid.

Claims (39)

1 . A pyrolysis process comprising:

introducing one or more chemical reactants into a reactor containing a liquid maintained at a high temperature, wherein the one or more chemical reactants are molecules containing carbon and hydrogen;

producing chemical products in the liquid based on the high temperature, wherein the chemical products comprise a solid product that is mixed with the liquid;

allowing the solid product to grow in particle size;

accumulating the solid product in the liquid;

pneumatically conveying the solid product from the reactor, while retaining a substantial portion of the liquid within the reactor, via a gas stream introduced into a head space of the reactor;

separating the solid product from the liquid reaction medium on a grate in an upper connection of the reactor; and

pneumatically conveying the solid product from the grate to remove the solid product from the reactor.

2 . The process of claim 1 , wherein the reactor is a bubble column.

3 . The process of claim 1 , wherein the high temperature is between 400° C. and 1500° C.

4 . The process of claim 1 , wherein the liquid is a molten salt, a molten metal, or a combination of a molten salt and a molten metal.

5 . The process of claim 1 , wherein the carbon and hydrogen containing reactants are decomposed to form solid carbon, wherein the solid carbon aggregates and grows within the liquid to form particles greater than 1 micrometer in size.

6 . The process of claim 1 , further comprising: accumulating the solid product on the top of the liquid surface via flotation.

7 . The process of claim 1 , further comprising: using a filter to separate the solid product from the liquid.

8 . The process of claim 1 , wherein pneumatically conveying the solid product from the reactor comprises: introducing an auxiliary gas stream into the reactor to convey the solid product out of the reactor.

9 . The process of claim 1 , wherein pneumatically conveying the solid product from the reactor comprises:

entraining the solid product in a pneumatically conveying gas stream; and

removing the solid product from the reactor based on the entraining.

10 . The process of claim 7 , further comprising:

separating the solid product from the pneumatically conveying gas stream.

11 . The process of claim 1 , wherein the reactor comprises a main reaction section, a side leg, the upper connection between the main reaction section and the side leg, and a lower connection between the main reaction section and the side leg.

12 . The process of claim 1 , further comprising:

flowing the liquid reaction medium and at least a portion of the solid product through the upper connection.

13 . The process of claim 1 , further comprising:

separating the solid product from the pneumatically conveying gas stream.

14 . A pyrolysis system comprising:

chemical reactants, wherein the chemical reactants comprise molecules containing carbon and hydrogen;

a reactor comprising a molten liquid;

chemical products disposed in the molten liquid, wherein the chemical products comprise a solid product that is mixed with the liquid;

a gas stream inlet disposed in the reactor, wherein the gas stream inlet is configured to pneumatically convey the solid product from the reactor using a gas stream while retaining a substantial portion of the liquid within the reactor; and

a grate disposed in an upper connection of the reactor; wherein the gas stream inlet is configured to pneumatically convey the solid product from the grate to remove the solid product from the reactor.

15 . The system of claim 14 , wherein the molten liquid is a molten salt, a molten metal, or a combination of a molten salt and a molten metal.

16 . The system of claim 14 , wherein the solid product comprises carbon particles greater than 1 micrometer in size.

17 . The system of claim 14 , wherein the solid product is disposed on the top of the molten liquid surface.

18 . The system of claim 14 , further comprising: a filter configured to separate the solid product from the molten liquid.

19 . The system of claim 14 , further comprising:

a separator in fluid communication with the reactor, wherein the separator is configured to receive the gas stream with the solid product and separate the solid product from the pneumatically conveying gas stream.

20 . The system of claim 14 , wherein the reactor is a bubble column.

21 . The system of claim 14 , wherein the reactor comprises a main reaction section, a side leg, the upper connection between the main reaction section and the side leg, and a lower connection between the main reaction section and the side leg.

Assignments (4)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 10, 2026
From: CZERO, INC.
To: MOLTEN INDUSTRIES INC.
Reel/Frame 073751/0295 →
RELEASE OF SECURITY INTEREST Recorded Aug 27, 2024
From: BERYLLIUM CAPITAL, L.L.C.
To: CZERO, INC.
Reel/Frame 068414/0982 →
SECURITY INTEREST Recorded Jul 30, 2024
From: CZERO, INC.
To: BERYLLIUM CAPITAL L.L.C.
Reel/Frame 068124/0034 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 10, 2023
From: SHANER, SAMUEL; JONES, ZACHARY; CALDWELL, ANDREW; SAADI, FADL
To: CZERO, INC.
Reel/Frame 062325/0624 →
Continuity (2)
Provisional Application 62989016 · Mar 13, 2020
Related Publication 20230099516A1 · Mar 30, 2023
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