System for effluent stream abatement via pyrolytic emission looping

Patent metadata

Field	Value
Publication number	US-12522773-B2
Application number	US-202318198723-A
Country	US
Kind code	B2
Filing date	May 17, 2023
Priority date	May 17, 2023
Publication date	Jan 13, 2026
Grant date	Jan 13, 2026

Abstract

Pyrolytic emissions often include molecularly decomposed hydrocarbons, as well as byproducts from pyrolytic processes. Unfortunately, legacy processing treats effluent streams, including pyrolytic emissions, as waste that is released into the air-even though such pyrolytic emissions streams often include greenhouse gases and pollutants such as carbon dioxide, nitrogen oxides, sulfur dioxide, volatile organic compounds, and particulate matter-the discharge of which contributes to global greenhouse gas emissions. Disclosed herein are pyrolytic emissions looping systems that include several reactors where each of the several reactors converts different hydrocarbons into different useful end-products, thus providing a way to continuously recycle the effluent gas stream from pyrolytic processes.

First claim

What is claimed is:

1 . A pyrolytic emissions looping system, including:
a feed gas stream; at least one dissociating reactor that receives the feed gas stream, and that outputs, at least in part, a first carbon allotrope material and a discharge pyrolytic emissions stream resulting from a pyrolytic decomposition; a gas separating system to separate the discharge pyrolytic emissions stream into at least one species component, wherein the separation includes processing of multiple types of hydrocarbons; a pyrolytic emissions waste gas stream comprising the at least one species component; and at least one second dissociating reactor that receives at least a portion of the pyrolytic emissions waste gas stream, wherein:
the at least one second dissociating reactor is a furnace reactor;
the at least one second dissociating reactor is configured to dissociate hydrocarbons and form a second carbon allotrope material different from the first carbon allotrope material; and
at least one of:
the at least one second dissociating reactor comprises a furnace reactor configured to transmute non-condensable components of the pyrolytic emissions waste gas stream into the second carbon allotrope material, or
the first carbon allotrope material comprises primary hydrocarbons derived from methane or compressed natural gas, and the second carbon allotrope material comprises secondary hydrocarbons derived from non- condensable polycyclic aromatic hydrocarbons.

2 . The pyrolytic emissions looping system of claim 1 , wherein the discharge pyrolytic emissions stream includes molecularly decomposed hydrocarbons.

3 . The pyrolytic emissions looping system of claim 1 , wherein the discharge pyrolytic emissions stream includes emission byproducts from a pyrolytic process.

4 . The pyrolytic emissions looping system of claim 1 , wherein the at least one species component is further added to the feed gas stream.

5 . The pyrolytic emissions looping system of claim 1 , wherein the pyrolytic emissions include a thermal decomposition, and the thermal decomposition includes a decomposition of at least one hydrocarbon.

6 . The pyrolytic emissions looping system of claim 1 , wherein the gas stream includes one or more polycyclic aromatic hydrocarbons, comprising at least one of: 1,3-Butadiene; 2,2,4-Trimethylpentane; 2-Propanol (IPA); 2-methylpentane; 4H-Cyclopenta[def]phenanthrene; Acetone; Acetylene; Acrylonitrile; Allylchloride; Benzene; Benzo[c]phenanthrene; Benzo[e]pyrene; Benzo[ghi]perylene; Benzo[ghi]perylene, 4-methyl-; Benzo[k]fluoranthene; Bicyclo[4.4.1]undeca-1,3,5,7,9-pentaene; Butadiene; Butane; Butenes; C4H10; C5H12; C6H14; Chlorobenzene; Coronene; Coronene, methyl-; Ethane; Ethylbenzene; Ethylene; Fluorene; HCN; Hexane +; Indeno[1,2,3-cd]pyrene; Isobutane; Isopentane; Isopropyl benzene; Isopropylbenzene; MEK; Methane; Methanol; Methylcyclohexane; Naphthalene; Naphthalene, 2-methyl-; Pentane; Phenanthrene; Propane; Propene; Propylene; Pyrene; Pyrene, 1-methyl-; Styrene; Toluene; m & p Xylene; n-butane; n-hexane; n-pentane; o,m&p-Xylenes; or o-Xylene.

7 . The pyrolytic emissions looping system of claim 5 , wherein the thermal decomposition occurs in the absence of oxygen.

8 . The pyrolytic emissions looping system of claim 1 , wherein the at least one species component includes at least one of Ar, N 2 , H 2 , CH 4 , O 2 , CO 2 , or one or more polycyclic aromatic hydrocarbons, comprising at least one of: 1,3-Butadiene; 2,2,4-Trimethylpentane; 2-Propanol (IPA); 2-methylpentane; 4H-Cyclopenta[def]phenanthrene; Acetone; Acetylene; Acrylonitrile; Allylchloride; Benzene; Benzo[c]phenanthrene; Benzo[e]pyrene; Benzo[ghi]perylene; Benzo[ghi]perylene, 4-methyl-; Benzo[k]fluoranthene; Bicyclo[4.4.1]undeca-1,3,5,7,9-pentaene; Butadiene; Butane; Butenes; C4H10; C5H12; C6H14; Chlorobenzene; Coronene; Coronene, methyl-; Ethane; Ethylbenzene; Ethylene; Fluorene; HCN; Hexane +; Indeno[1,2,3-cd]pyrene; Isobutane; Isopentane; Isopropyl benzene; Isopropylbenzene; MEK; Methane; Methanol; Methylcyclohexane; Naphthalene; Naphthalene, 2-methyl-; Pentane; Phenanthrene; Propane; Propene; Propylene; Pyrene; Pyrene, 1-methyl-; Styrene; Toluene; m & p Xylene; n-butane; n-hexane; n-pentane; o,m&p-Xylenes; or o-Xylene.

9 . The pyrolytic emissions looping system of claim 8 , wherein at least a portion of the at least one species component is an input stream to at least one of:
a proton exchange membrane fuel cell, the at least one dissociating reactor; the at least one second dissociating reactor; a third dissociating reactor, a power generation turbine, a catalytic converter, an oxidizer, or a CO 2 cracker.

10 . The pyrolytic emissions looping system of claim 1 , wherein the at least one dissociating reactor is configured to dissociate hydrocarbons.

11 . The pyrolytic emissions looping system of claim 10 , wherein the at least one dissociating reactor is configured to dissociate the hydrocarbons and form at least the first carbon allotrope material.

12 . The pyrolytic emissions looping system of claim 11 , wherein the gas separating system includes a cold trap and a multi-stage gas separator.

13 . The pyrolytic emissions looping system of claim 11 , further comprising at least one third dissociating reactor that receives an output of the gas separating system, wherein the at least one third dissociating reactor is configured to dissociate the hydrocarbons and form at least a third carbon allotrope material different from each of the first carbon allotrope material and the second carbon allotrope material.

14 . The pyrolytic emissions looping system of claim 1 , wherein the pyrolytic emissions looping system is configured for a hydrocarbon site, wherein the hydrocarbon site includes at least one of oil field, gas field, oil sand, oil shale deposit, coal deposit, offshore oil reserve, offshore gas reserve, shale gas deposit, methane hydrates, oil seep, or gas seep.

15 . The pyrolytic emissions looping system of claim 1 , wherein the at least one dissociating reactor is configured for a remote hydrocarbon site, and at least one of the following provisos are satisfied:
wherein the separation into at least one species component at the remote hydrocarbon site is configured for hydrocarbon reduction, wherein the separation into at least one species component at the remote hydrocarbon site is configured for hydrocarbon abatement, or wherein the separation into at least one species component reduces discharge of greenhouse gases.

16 . The pyrolytic emissions looping system of claim 1 , wherein at least one of the at least one dissociating reactor or the at least one second dissociating reactor includes a thermal reactor.

17 . The pyrolytic emissions looping system of claim 1 , wherein at least one of the at least one dissociating reactor or the at least one second dissociating reactor includes a microwave reactor.

18 . The pyrolytic emissions looping system of claim 1 , wherein all of the at least one species component is reused by the pyrolytic emissions looping system.

19 . The pyrolytic emissions looping system of claim 1 , wherein at least one of the at least one species component is reused by the pyrolytic emissions looping system.

20 . The pyrolytic emissions looping system of claim 1 , wherein the furnace reactor is one of a plasma reactor, a pulsed reactor, or a microwave reactor.

21 . The pyrolytic emissions looping system of claim 1 , wherein the first carbon allotrope material includes p

Assignees

• Lyten Inc

Inventors

• Sumabat Joshua
• Anzelmo Bryce H
• Cruz Joe

Classifications

• C10G2300/4062

  Geographical aspects, e.g. different process units form a combination process at different geographical locations · CPC title

• C10G2300/4081

  Recycling aspects · CPC title

• C10G2300/1033

  Oil well production fluids · CPC title

• C10G2300/201

  Impurities · CPC title

• C10G70/043 Primary

  by fractional condensation · CPC title