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Patent 3185797 Summary

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(12) Patent Application: (11) CA 3185797
(54) English Title: INCOMPLETE COMBUSTION AS A MEANS OF REDUCING CARBON DIOXIDE EMISSIONS
(54) French Title: COMBUSTION INCOMPLETE EN TANT QUE MOYEN DE REDUCTION DES EMISSIONS DE DIOXYDE DE CARBONE
Status: Report sent
Bibliographic Data
(51) International Patent Classification (IPC):
  • C25B 1/04 (2021.01)
(72) Inventors :
  • UMEALU, SAMUEL OKECHUKWU (Australia)
(73) Owners :
  • UMEALU, SAMUEL OKECHUKWU (Australia)
(71) Applicants :
  • UMEALU, SAMUEL OKECHUKWU (Australia)
(74) Agent: BSAT DESNOO, SUZAN
(74) Associate agent:
(45) Issued:
(86) PCT Filing Date: 2021-03-06
(87) Open to Public Inspection: 2022-03-24
Examination requested: 2023-01-11
Availability of licence: N/A
(25) Language of filing: English

Patent Cooperation Treaty (PCT): Yes
(86) PCT Filing Number: PCT/AU2021/000024
(87) International Publication Number: WO2022/056573
(85) National Entry: 2023-01-11

(30) Application Priority Data:
Application No. Country/Territory Date
2021201303 Australia 2021-02-28

Abstracts

English Abstract

What is disclosed herein is a process for the elimination Carbon dioxide (CO2), exploiting renewable energy sources, providing storage for intermittent renewable power and production of synthesis gas, a fuel gas mixture consisting primarily of carbon monoxide (CO) and hydrogen (H2), which is then utilised in the Fischer-Tropsch reaction to produce clean fuels and other chemical solvents.


French Abstract

La divulgation concerne un procédé d'élimination du dioxyde de carbone (CO2), l'exploitation de sources d'énergie renouvelable, la fourniture d'un stockage pour une énergie renouvelable intermittente et la production d'un gaz de synthèse, d'un mélange de gaz combustible constitué principalement de monoxyde de carbone (CO) et d'hydrogène (H2), qui est ensuite utilisé dans la réaction de Fischer-Tropsch pour produire des carburants propres et d'autres solvants chimiques.

Claims

Note: Claims are shown in the official language in which they were submitted.


Claims
What is claimed is:
Claim 1
A process for using incomplete combustion of fossil fuel is a power plant to
generate
electricity, with the CO component of the flue gas transferred to a Fischer-
Tropsch
reactor, with the 1120 component of the flue gas transferred to an
Electrolysis machine
where it is split into H2 and 02. and the resulting H2 is also transfeired to
the same
Fischer-Tropsch reactor that contains the CO component of the flue gas where a

renewable fuel is created and some of it recycled to the power plant.
Claim 2
The method of claim 1, wherein carbon rnonoxide (CO) is recovered from the
flue gas
Claim 3
The method of claim 1, wherein carbon (C) is recovered from the flue gas and
re-cycled
to the first step of incomplete combustion.
Claim 4
The method of claim 1, wherein E120 is split into 112 and 02
Claim 5
The method of claim 1, wherein renewable energy sources including Biofuel,
Biomass,
Geothermal, Hydroelectricity, Solar, Wind, Tidal and Wave are used in
electrolysis to
split H20 into H2 and Oz
Claim 6
The method of claim 1, wherein the use of renewable energy sources including
Biofuel,
Biomass, Geothermal, Hydroelectricity, Solar, Wind, Tidal and Wave in
electrolysis to
split H20 into H2 and 02 is considered rneans of exploiting these renewable
energy
sources.
CA 03185797 2023- 1- 11

Claim7
The method of claim 1, wherein the use of intermittent renewable energy
sources
including Geothermal, Hydroelectricity, Solar, Wind, Tidal and Wave in the
electrolysis
of H20 to produce hydrogen (HI) is considered means of storing power from
these
intermittent energy sources.
Claim8
The method of claim 1, wherein the use of renewable energy sources including
Biofuel,
Biomass, Geothermal, Hydroelectricity, Solar, Wind, Tidal and Wave in the
electrolysis
of H20 to produce hydrogen (H2) is considered means of converting these
renewable
energy sources to chemical energy.
Claim9
The method of claims 1 , wherein carbon monoxide (CO) resulting from claiin 2
and
hydrogen (H?), resulting from 4 are used in Fischer-Tropsch reaction to
produce
renewable ftiels and chemical solvents
Claim 10
The method of claim 1, wherein some of the renewable fuels of claim 9 are
recycled to
the first step of incomplete combustion.
Claim 11
The method of claim 1, wherein the energy output of the Fischer-Tropsch
reaction is
recovered recycled to the first step of incomplete combustion.
6
CA 03185797 2023- 1- 11

Description

Note: Descriptions are shown in the official language in which they were submitted.


WO 2022/056573
PCT/AU2021/000024
The title of the invention: INCOMPLETE COMBUSTION AS A MEANS OF
REDUCING CARBON DIOXIDE EMISSIONS
Background of the Invention
[001] Carbon dioxide (CO2) has a significant impact on global warming.
[002] Emissions of Carbon dioxide (C0z) arise from a number of sources, mainly
fossil
fuel combustion to generate energy. Fossil fuel comprises Coal and
hydrocarbons.
[003] Emissions of Carbon dioxide (CO2) arise from complete combustion of
fossil fuel,
according to the following equation:
Fossil Fuel + Oxygen(02) ¨> Carbon dioxide (CO2) + Water (H20) + Flue Gas
Mixture
The source of oxygen for this reaction is the atmospheric air.
[004] Carbon monoxide (CO) is produced instead of Carbon dioxide (CO2) in
incomplete
combustion. Incomplete combustion happens when there is a limited supply of
air,
according to the following equation:
Fossil Fuel + Oxygen(02) ¨> Carbon monoxide (CO) + Water (H20) + Carbon(C)
[005] Water splitting is the chemical reaction in which water is broken down
into oxygen
and hydrogen, according to the following equation:
2 H20 ¨> 2 H2 02
It is, in other words, electrolysis of water or the decomposition of water (1-
120) into
oxygen (02) and hydrogen (H2), due to an electric current being passed through
it.
Production of hydrogen from water is energy intensive. In low-temperature
electrolysis,
the energy consumed is more valuable than the hydrogen produced. Therefore,
this
process is not usually considered commercially viable. I Iowever, with high-
temperature
electrolysis (HTE) of water, more of the initial heat energy is converted into
chemical
energy (hydrogen), thereby improving the commercial viability of this process.
The
commercial viability of this process is further improved by use of renewable
energy
sources to generate electricity for electrolysis.
[006] The use of renewable energy sources in the electrolysis of water
provides means of
exploiting these renewable energy sources. It also provides means of storing
intermittent
renewable power by conversion to chemical energy in hydrogen_
[007] The Fischer-Tropsch is a reaction involving carbon monoxide (CO) and
hydrogen
(H2) to produce clean fuels and other chemical solvents.
1
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WO 2022/056573
PCT/AU2021/000024
Detailed Description of the Invention
[001] This invention transforms fuels such as coal and other hydrocarbons from
"dirty" to
:'clean" source of energy. Future power plants may use fossil fuels or the so-
called dirty
fuels to generate Clean energy by using this invention. Existing power plants
that
currently use fossil fuels as feedstock can be amended to commence generation
of Clean
energy by using this invention.
[002] This invention provides the means of harnessing renewable energy
sources. It is
also a viable solution to the problem of intermittent renewable power storage.
[003] This invention provides a "clean" source of cheap commercial scale
synthesis gas,
a fuel gas mixture consisting primarily of carbon monoxide (CO) and hydrogen
(H2).
The fuel gas mixture is used to produce hydrocarbons in a Fischer-Tropsch
process.
[004] These together with additional objects, features and advantages of the
incomplete
combustion as a means of reducing Carbon Dioxide emissions will be readily
apparent to
those of ordinary skill in the art upon reading the following detailed
description of the
presently preferred, but nonetheless illustrative, embodiments when taken in
conjunction
with the accompanying drawings.
[005] In this respect, before explaining the current embodiments of the
incomplete
combustion as a means of reducing Carbon Dioxide emissions in detail, it is to
be
understood that the incomplete combustion as a means of reducing Carbon
Dioxide
emissions is not limited in its applications to the details of design,
construction and
arrangements of the components set forth in the following description. Those
skilled in
the art will appreciate that the concept of this disclosure may be readily
utilized as a basis
for the design of other processes, structures, methods, and systems for
carrying out the
several purposes of the incomplete combustion as a means of reducing Carbon
Dioxide
emissions. It is therefore important that the claims be regarded as including
such
equivalent construction insofar as they do not depart from the spirit and
scope of the
incomplete combustion as a means of reducing Carbon Dioxide emissions. It is
also to be
understood that the phraseology and terminology employed herein are for
purposes of
description and should not be regarded as limiting.
[006] The following detailed description is merely exemplary in nature and is
not
intended to limit the described embodiments of the application and uses of the
described
embodiments_ As used herein, the word "exemplary" or "illustrative" means
"serving as
2
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WO 2022/056573
PCT/AU2021/000024
an example, instance, or illustration." Any implementation described herein as

"exemplary" or "illustrative" is not necessarily to be construed as preferred
or
advantageous over other implementations. All of the implementations described
below
arc exemplary implementations provided to enable persons skilled in the art to
practice
the disclosure and are not intended to limit the scope of the appended claims.

Furthermore, there is no intention to be bound by any expressed or implied
theory
presented in the preceding technical field, background or the following
detailed
description.
[007] This invention provides a viable solution to the problem of global
warming as
caused by Carbon dioxide (CO2) emissions arising from fossil fuel combustion
to
generate energy. In step 1 of the process, this invention uses incomplete
combustion to
ensure an output of carbon monoxide (CO) and water (H20), instead of Carbon
dioxide
(CO2) and Water (F120), as would have been the case if complete combustion
were used.
[008] In step 3 of the process, carbon monoxide (CO), water (H20) and carbon
(C) are
separated. Carbon monoxide (CO), a valuable component of synthesis is sent to
step 5
where it takes part in Fischer-Tropsch reaction, in which fossil fuel in the
form of
hydrocarbon is produced. Carbon (C) is recycled to step 1, while water (H20)
is sent to
step 4, where it is used as feedstock for high-temperature electrolysis (HTE).
[009] In step 4 of the process, water (H20) from step 3 is made to undergo
high-
temperature electrolysis (ME), by using renewable power. This high-temperature

electrolysis (HTE) results in the generation of hydrogen (H2). The use of
renewable
power in this step to generate hydrogen (H2) translates to conversion of these
renewable
energy supply to chemical energy. Hydrogen (H2) is a valuable component of
synthesis
gas and will be used in step 5, along with Carbon monoxide (CO) to create
fossil fuel, in
the form of hydrocarbons. Conversion of renewable energy to chemical energy
provides a
viable solution to the problem of intermittent renewable power storage.
[010] Renewable energy sources include Biofuel, Biomass, Geothermal,
Hydroelectricity,
Solar, Wind, Tidal and Wave. Some of these energy sources are known to produce

intermittent power.
[011] This invention results in the production of synthesis gas, a fuel gas
mixture
consisting primarily of carbon monoxide (CO) and hydrogen (H2), in steps 1 and
4,
respectively. These two gases (carbon monoxide (CO) and hydrogen (H2)) are
made to
3
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WO 2022/056573
PCT/AU2021/000024
undergo the Fischer-Tropsch reaction in step 5, to produce clean fuels and
other chemical
solvents. Some of the resulting fuels is recycled to step 1.
[012] According to Vvrikipedia, the Fischer¨Tropsch process is a collection of
chemical
reactions that converts a mixture of carbon monoxide and hydrogen into liquid
hydrocarbons. These reactions occur in the presence of metal catalysts,
typically at
temperatures of 150-300 C (302-572 F) and pressures of one to several tens
of
atmospheres. The process was first developed by Franz Fischer and Hans Tropsch
at the
Kaiser-Wilhelm-Institut fur Kohlenforschung in Germany, in 1925.
[013]With respect to the above description, it is to be realized that the
optimum
dimensional relationship for the various components of the invention described
above
and in following drawing include variations in size, materials, shape, form,
function, and
manner of operation, assembly and use, are deemed readily apparent and obvious
to one
skilled in the art, and all equivalent relationships to those illustrated in
the drawings and
described in the specification are intended to be encompassed by the
invention.
[014] It shall be noted that those skilled in the art will readily recognize
numerous
adaptations and modifications which can be made to the various embodiments of
the
present invention which will result in an improved invention, yet all of which
will fall
within the spirit and scope of the present invention as defined in the
following claims.
Accordingly, the invention is to be limited only by the scope of the following
claims and
their equivalents.
BRIEF DESCRIPTION OF DRAWINGS
The accompanying drawing, which is included to provide a further understanding
of the
invention is incorporated in and constitute a part of this specification,
illustrate an
embodiment of the invention and together with the description serve to explain
the
principles of the invention. They are meant to be exemplary illustrations
provided to
enable persons skilled in the art to practice the disclosure and are not
intended to limit the
scope of the appended claims.
4
SUBSTITUTE SHEET (RULE 26) RO/AU
CA 03185797 2023- 1- 11

Representative Drawing
A single figure which represents the drawing illustrating the invention.
Administrative Status

For a clearer understanding of the status of the application/patent presented on this page, the site Disclaimer , as well as the definitions for Patent , Administrative Status , Maintenance Fee  and Payment History  should be consulted.

Administrative Status

Title Date
Forecasted Issue Date Unavailable
(86) PCT Filing Date 2021-03-06
(87) PCT Publication Date 2022-03-24
(85) National Entry 2023-01-11
Examination Requested 2023-01-11

Abandonment History

There is no abandonment history.

Maintenance Fee

Last Payment of $50.00 was received on 2023-01-11


 Upcoming maintenance fee amounts

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Next Payment if small entity fee 2024-03-06 $50.00
Next Payment if standard fee 2024-03-06 $125.00

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Payment History

Fee Type Anniversary Year Due Date Amount Paid Paid Date
Application Fee $210.51 2023-01-11
Maintenance Fee - Application - New Act 2 2023-03-06 $50.00 2023-01-11
Request for Examination 2025-03-06 $408.00 2023-01-11
Owners on Record

Note: Records showing the ownership history in alphabetical order.

Current Owners on Record
UMEALU, SAMUEL OKECHUKWU
Past Owners on Record
None
Past Owners that do not appear in the "Owners on Record" listing will appear in other documentation within the application.
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National Entry Request 2023-01-11 1 22
Miscellaneous correspondence 2023-01-11 2 41
Miscellaneous correspondence 2023-01-11 1 16
Miscellaneous correspondence 2023-01-11 1 15
Voluntary Amendment 2023-01-11 3 69
Representative Drawing 2023-01-11 1 17
Patent Cooperation Treaty (PCT) 2023-01-11 1 52
Description 2023-01-11 4 196
Drawings 2023-01-11 1 12
International Search Report 2023-01-11 3 97
Patent Cooperation Treaty (PCT) 2023-01-11 1 62
Correspondence 2023-01-11 2 49
Abstract 2023-01-11 1 10
National Entry Request 2023-01-11 8 228
Claims 2023-01-11 2 54
Special Order - Green Granted 2023-03-23 1 167
Claims 2023-01-12 2 55
Cover Page 2023-05-31 1 38
Examiner Requisition 2024-04-04 4 168
Office Letter 2024-03-28 2 189