WV Coal Member Meeting 2024 1240x200 1 1

July, 2012, CO2 to Methanol

United   States Patent Application: 0120171583

We've documented many times that the potential exists for what is,   essentially, the electrolysis of Carbon Dioxide, or co-electrolysis of CO2   with a co-reactant, usually H2O, a process sometimes referred to as   "syntrolysis", in order to chemically reduce or recombine Carbon Dioxide,   and/or it's co-reactants, into more active chemical species.
An early example of such technology was developed at one of our US   National Laboratories, as seen in:

West   Virginia Coal Association | USDOE 1976 Atmospheric CO2 to Methanol | Research   & Development; concerning: "United States Patent 3,959,094 -   Electrolytic Synthesis of Methanol from CO2; 1976; Assignee: The USA as   represented by the USDOE; Abstract: A method and system for synthesizing   methanol from the CO2 in air using electric power. The CO2 is absorbed by a   solution of KOH to form K2CO3 which is electrolyzed to produce methanol, a   liquid hydrocarbon fuel".

Such reactions take quite a bit of energy, electrical power, to   drive them forward; and, efforts were subsequently made to, one way or   another, reduce the power demand; as seen, for one example, in:

West   Virginia Coal Association | Texaco Recycles More CO2 to Methanol and Methane |   Research & Development; concerning: "United States Patent 4,609,451 -   Means for Reducing Carbon Dioxide to Provide a Product; 1986; Assignee: Texaco   Incorporated; Abstract: A process and apparatus for reducing carbon   dioxide to at least one useful product includes two redox couple electrolyte   solutions separated by a first membrane having photosensitizers. The carbon   dioxide to be reduced is provided to a second membrane whch is contiguous to   one of the redox couple electrolyte solutions. The second membrane has   photosensitizers and a catalyst. Water provides hydrogen ions, which   participate in the reduction of the carbon dioxide, via a separator. In   operation both membranes are illuminated and produce excited photosensitizers   which cause electron transfer from a first redox solution to a second redox   solution and thence to the carbon dioxide in the second membrane thereby, in   cooperation with the hydrogen ions, reducing at least some of the carbon   dioxide at a surface of the second membrane to provide at least one product.   The present invention relates to photoelectrical chemical methods and   apparatus for reducing carbon dioxide ... to at least one useful product   (which) includes two redox couple electrolyte solutions separated by a   first membrane having photosensitizers. The carbon dioxide to be reduced is   provided to a second membrane which is contiguous to one of the redox couple   electrolyte solutions. The second membrane has photosensitizers and a   catalyst";

wherein light energy and "a catalyst" are employed to reduce the electric   potential needed to chemically reduce Carbon Dioxide and drive it's   recombination with other reactants.

Thermal energy, too, can be employed for that purpose, as also   demonstrated by the USDOE, and their corporate partners, as seen for one   example in:

West   Virginia Coal Association | More USDOE CO2 "Syntrolysis" | Research &   Development; concerning: 

"Co-Electrolysis of Steam and Carbon Dioxide for Production of Syngas;   2007; Idaho National Laboratory, USDOE; and Ceramatec, Inc., Utah; Abstract:   An experimental study has been completed to assess the performance of   single-oxide electrolysis cells ... simultaneously electrolyzing steam and   carbon dioxide for the direct production of syngas. Syngas, a mixture of   hydrogen and carbon monoxide, can be used for the production of synthetic   liquid fuels via Fischer-Tropsch processes";

wherein H2O is first converted into Steam; and, the Steam and the CO2 are   then "co-electrolyzed".

We've previously reported that rather extensive developments in such   energized and catalyzed processes for the co-conversion of CO2 and H2O have   also been established at the Princeton University labs of Professor   Andrew Bocarsly, as seen, for instance, in:

West   Virginia Coal Association | Princeton Recycles CO2 with US Government Support   | Research & Development; concerning: "US Patent Application   20100187123A1 - Conversion of Carbon Dioxide to Organic Products; 2010;   Inventors: Andrew B. Bocarsly and Emily Barton Cole, NJ; Government Interests:   This invention was made with United States government support from Natural   Science Foundation Grant No. CHE-0606475. The United States Government has   certain rights in this invention. The invention relates to various embodiments   of an environmentally beneficial method for reducing carbon dioxide. The   methods in accordance with the invention include electrochemically or   photoelectrochemically reducing the carbon dioxide in a divided   electrochemical cell (with) a catalyst of one or more substituted or   unsubstituted aromatic amines to produce therein a reduced organic product.   Claims: A method of converting of carbon dioxide to provide at least one   product, comprising reducing the carbon dioxide in a divided electrochemical   cell ... . (And) wherein the reducing is electrochemical or   photoelectrochemical (and) where the at least one product is methanol,   isopropanol, formic acid, formaldehyde, glyoxal or ethanol".

And, note that, as we explained more fully in our report of:

West   Virginia Coal Association | Princeton Scientists Convert More CO2 to Methanol   and Ethanol | Research & Development; concerning: "United States   Patent Application 20110114502 - Reducing Carbon Dioxide to Products; 2011;   Inventors: Emily Barton Cole (and) Andrew Bocarsly, et. al., NJ, DC and   CA"; 

Princeton scientists Bocarsly and Cole have joined forces with other   like-mined scholars to form the company, "Liquid Light", as explained   via:

Liquid Light :: About; "Liquid Light is   uniquely developing a low-cost, energy-efficient system to convert CO2 into a   wide variety of chemicals and liquid fuels using clean energy sources. Through its patent-pending catalytic   platform originated from the renowned research lab of Professor Andrew   Bocarsly at Princeton University, the Company’s carbon conversion approach   incorporates low-cost inputs with long-term pricing predictability, reduces   capital expenditures by going direct from CO2 to the final product, achieves   energy efficiency through its particular catalysts, and offers selective   conversion to a desired end product. Additionally, its process leverages   secure, clean, domestic sources of energy with reduced emissions, and can   store intermittent clean energy as liquid fuels. The Company is based in   New Jersey with a core team from the likes of DARPA and the labs of the DOE,   Berkeley, and Princeton. They are supported by leading experts in the fields   of catalysis and carbon dioxide utilization".

And, herein, we learn that Princeton's Andrew Bocarsly and a few of   his other colleagues, have "merged" some of the prior art Carbon Dioxide   chemical reduction and conversion technology, as outlined in general by   our references to prior reports, and recently applied for a United States   Patent on what we see as something of a consolidated technology for recycling   CO2.

As seen, with notes and comment inserted and appended, in excerpts from   the initial link in this dispatch to:

"United States Patent Application 20120171583 - Gas Phase Electrochemical   Reduction of Carbon Dioxide

(GAS PHASE   ELECTROCHEMICAL REDUCTION OF CARBON DIOXIDE - LIQUID LIGHT, INC.)

Date: July 5, 2012

Inventors: Andrew Bocarsly, et. el., NJ and IL

Assignee: Liquid Light, Inc., NJ

Abstract: Methods and systems for gas phase electrochemical reduction of   carbon dioxide are disclosed. A method for gas phase electrochemical reduction   of carbon dioxide may include, but is not limited to, steps (A) to (C). Step   (A) may include introducing a substantially gas phase fuel to an anode flow   field of an anode of a proton exchange membrane (PEM) fuel cell. Said anode   may be a gas diffusion electrode. Step (B) may include introducing a   substantially gas phase carbon dioxide to a cathode flow field of a cathode of   said PEM fuel cell. Said cathode may be a chemically modified gas diffusion   electrode including a coating of a polymer aromatic amine. Step (C) may   include reducing at least a portion of said substantially gas phase carbon   dioxide to a product mixture at said cathode.

(Note the term "fuel cell". A number of emerging CO2 recycling   technologies seem to spring from the concept of running a fuel cell "in   reverse", so to speak, using Carbon-free environmental energy to drive the   processes. Another example of such "reverse fuel cell" technology is seen in   our report concerning the USDOE's "syntrolysis" partner, as in our above-cited   report concerning "Co-Electrolysis of Steam and Carbon Dioxide for Production   of Syngas", the Utah company, Ceramatec:

West   Virginia Coal Association | Utah 2011 CO2 + H2O = Hydrocarbon Syngas |   Research & Development; concerning: "United States Patent 8,075,746 -   Electrochemical Cell for Production of Synthesis Gas Using Atmospheric Air and   Water; Date: December 13, 2011; Assignee: Ceramatec, Inc., Salt Lake City;   Abstract: A method is provided for synthesizing synthesis gas from carbon   dioxide obtained from atmospheric air or other available carbon dioxide source   and water using a sodium-conducting electrochemical cell. Synthesis gas is   also produced by the coelectrolysis of carbon dioxide and steam in a solid   oxide fuel cell or solid oxide electrolytic cell. The synthesis gas produced   may then be further processed and eventually converted into a liquid fuel   suitable for transportation or other applications".

Also, concerning the specified "gas diffusion electrode", see:

Gas diffusion   electrode - Wikipedia, the free encyclopedia.)

Claims: A method for gas phase electrochemical reduction of carbon   dioxide, comprising:

(A) introducing a substantially gas phase fuel to an anode flow field of   an anode of a proton exchange membrane (PEM) fuel cell, wherein said anode is   a gas diffusion electrode;

(Proton   exchange membrane fuel cell - Wikipedia, the free encyclopedia; "Proton   exchange membrane fuel cells, also known as polymer electrolyte membrane (PEM)   fuel cells (PEMFC), are a type of fuel cell being developed for transport   applications as well as for stationary fuel cell applications and portable   fuel cell applications. Their distinguishing features include lower   temperature/pressure ranges (50 to 100 °C) and a special polymer electrolyte   membrane. They are a leading candidate to replace the aging alkaline fuel cell   technology, which was used in the Space Shuttle.")

(B) introducing a substantially gas phase carbon dioxide to a cathode   flow field of a cathode of said PEM fuel cell, wherein said cathode is a   chemically modified gas diffusion electrode including a coating of a polymer   aromatic amine; and;

(C) reducing at least a portion of said substantially gas phase carbon   dioxide to a product mixture at said cathode.

The method   ... where said coating of said polymer aromatic amine comprises a coating   of a pyridinium-containing polymer.

(Pyridinium - Wikipedia, the   free encyclopedia; "Pyridinium refers to (a) form of pyridine."

Pyridine - Wikipedia, the free   encyclopedia; "Pyridine is a basic heterocyclic organic compound   ... structurally related to benzene ... (and) occurs in many important   compounds, including ...  the vitamins niacin and pyridoxal. Pyridine was   discovered in 1849."

It is, in other words, easy to get.)

The method ...  wherein introducing a substantially gas phase   fuel to an anode flow field of an anode of a proton exchange membrane (PEM)   fuel cell comprises: introducing a humidified hydrogen stream to said anode   flow field of said anode of said PEM fuel cell.

(If we need Hydrogen, there are many ways to efficiently get some, as we   documented most recently in:

West   Virginia Coal Association | Japan Maximizes Hydrogen Production from Wind   Power | Research & Development; concerning: "United States Patent   7,667,343 - Hydrogen Production System Using Wind Turbine Generator; 2010;   Assignee: Hitachi, Ltd.;  A wind turbine-driven hydrogen production   system".

However, the reverse fuel cell "syntrolysis"-type technology employed by   the Idaho National Lab and Ceramatec, as per our above-cited references,   apparently doesn't require Hydrogen supplementation; it's all derived from the   H2O being co-reacted with the CO2. Adding Hydrogen as a supplement might   improve the efficiency of the process.)

The method ... wherein   introducing a substantially gas phase carbon dioxide to a cathode flow field   of a cathode of said PEM fuel cell comprises: introducing a humidified carbon   dioxide stream to said cathode flow field of said cathode of said PEM fuel   cell.

(The qualifier "humidified" means, of course, that it's mixed with H2O.)

The method ... wherein at least one of said gas   diffusion electrode of said anode or said chemically modified gas diffusion   electrode of said cathode includes a metal nanoparticle on carbon gas   diffusion electrode.

The method ... wherein said product   mixture includes at least one of methanol or propanol.

The method   ...  wherein said PEM fuel cell provides between approximately 30% to 95%   faradaic yield for methanol.

(The phrase "faradaic yield" equates with: Faraday efficiency -   Wikipedia, the free encyclopedia. And, "95%" is pretty darned good.)

A system for gas phase electrochemical reduction of carbon   dioxide, comprising: a fuel cell, including: an anode including a gas   diffusion electrode having an anode flow field; a cathode including a   chemically modified gas diffusion electrode having a coating of a polymer   aromatic amine; and a membrane electrode assembly positioned between said   anode and said cathode; a fuel source, said fuel source coupled with said   anode, said fuel source configured to supply a gaseous fuel to said anode flow   field; and a carbon dioxide input, said carbon dioxide input configured to be   coupled between a carbon dioxide source and said cathode, said carbon dioxide   input configured to provide gaseous carbon dioxide to said cathode flow field   for reduction of said gaseous carbon dioxide to a product mixture at said   cathode.

The system ... wherein said gaseous fuel includes   humidified hydrogen.

(Again, if we need supplemental Hydrogen, as seen   for another example in:

More   NASA Hydrogen from Water and Sunlight | Research & Development;   concerning: "United States Patent 4,051,005 - Photolytic Production of   Hydrogen; 1977; Assignee: United Technologies Corporation;

Government Interests: The invention described herein was made in the   course of a contract with the National Aeronautics and Space Administration.   Abstract: Hydrogen and oxygen are produced from water in a process involving   the photo-dissociation of molecular bromine with radiant energy at wavelengths   within the visible light region";

we can get it through the use of environmental energies, in ways that   shouldn't break the bank.)

Background and Field:  The present disclosure generally relates to   the field of electrochemical reactions, and more particularly to methods   and/or systems for gas phase electrochemical reduction of carbon dioxide.  

Countries around the world, including the United States, are seeking   ways to mitigate emissions of carbon dioxide.

A mechanism for   mitigating emissions is to convert carbon dioxide into economically valuable   materials such as fuels and industrial chemicals. If the carbon dioxide is   converted using energy from renewable sources, both mitigation of carbon   dioxide emissions and conversion of renewable energy into a chemical form that   can be stored for later use will be possible.

However, the field of   electrochemical techniques in carbon dioxide reduction has many limitations,   including the stability of systems used in the process, the efficiency of   systems, the selectivity of the systems or processes for a desired chemical,   the cost of materials used in systems/processes, the ability to control the   processes effectively, and the rate at which carbon dioxide is converted. In   particular, existing electrochemical and photochemical processes/systems have   one or more of the following problems that prevent commercialization on a   large scale. Several processes utilize metals, such as ruthenium or gold, that   are rare and expensive. In other processes, organic solvents were used that   made scaling the process difficult because of the costs and availability of   the solvents, such as dimethyl sulfoxide, acetonitrile, and propylene   carbonate. Copper, silver and gold have been found to reduce carbon dioxide to   various products, however, the electrodes are quickly "poisoned" by   undesirable reactions on the electrode and often cease to work in less than an   hour. Similarly, gallium-based semiconductors reduce carbon dioxide, but   rapidly dissolve in water. Many cathodes produce a mixture of organic   products. For instance, copper produces a mixture of gases and liquids   including carbon monoxide, methane, formic acid, ethylene, and ethanol. Such   mixtures of products make extraction and purification of the products costly   and can result in undesirable waste products that must be disposed. Much of   the work done to date on carbon dioxide reduction is inefficient because of   high electrical potentials utilized, low faradaic yields of desired products,   and/or high pressure operation. The energy consumed for reducing carbon   dioxide thus becomes prohibitive. Many conventional carbon dioxide reduction   techniques have very low rates of reaction.

Summary and Description: A method for gas phase electrochemical reduction   of carbon dioxide may include, but is not limited to, steps (A) to (C). Step   (A) may include introducing a substantially gas phase fuel to an anode flow   field of an anode of a proton exchange membrane (PEM) fuel cell. Said anode   may be a gas diffusion electrode. Step (B) may include introducing a   substantially gas phase carbon dioxide to a cathode flow field of a cathode of   said PEM fuel cell. Said cathode may be a chemically modified gas diffusion   electrode including a coating of a polymer aromatic amine. Step (C) may   include is reducing at least a portion of said substantially gas phase carbon   dioxide to a product mixture at said cathode.

The system may   further include a carbon dioxide input. Said carbon dioxide input may be   coupled between a carbon dioxide source and said cathode and may be configured   to supply gaseous carbon dioxide to said cathode flow field for reduction of   said gaseous carbon dioxide to a product mixture at said cathode.  

(An) electrochemical system is provided that generally allows   electrochemical reduction of carbon dioxide substantially in the gas phase,   thereby utilizing the greenhouse gas as a reactant to transfer the reaction   energy into a chemical form that can be stored for later use.

By facilitating the electrochemical reduction of carbon dioxide in the   gas phase, improved reaction rates (e.g., as measured by current density of   the electrochemical cell) may be achieved as compared to the reaction rate of   a liquid-based electrochemical system."

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And, don't forget, the "product mixture" obtained at up "to   95% faradaic yield", from recycled Carbon Dioxide, "includes at least one of   methanol or propanol".

Methanol, as seen in:

Mobil   Oil Coal to Methanol to Gasoline | Research & Development; concerning:   "United States Patent 4,447,310 - Production of Distillates through Methanol   to Gasoline; 1984; Assignee: Mobil Oil Corporation;

Abstract: A process for producing a wide slate of fuel products from coal   is provided by integrating a methanol-to-gasoline conversion process with coal   liquefaction and coal gasification. The coal liquefaction comprises contacting   the coal with a solvent under supercritical conditions whereby a dense-gas   phase solvent extracts from the coal a hydrogen-rich extract which can be   upgraded to produce a distillate stream. The remaining coal is gasified under   oxidation conditions to produce a synthesis gas which is converted to   methanol. The methanol is converted to gasoline by contact with a zeolite   catalyst. Solvent for coal extraction is process derived from the upgraded   distillate fraction or gasoline fraction of the methanol-to-gasoline   conversion";

no matter which of our abundant resources, Carbon Dioxide, as herein, or   Coal, we make it from, can be efficiently converted into Gasoline.

On the other hand, as seen in:

chemical   industry : Ethanol and its products -- Britannica Online Encyclopedia;   "The alcohol 2-propanol ... is manufactured on the million-ton scale. It is   made from propylene by a process similar to that used to convert ethylene to   ethanol, and manufacture of 2-propanol by this process initiated the   petrochemical industry in the 1920s. The principal use of 2-propanol   is in the manufacture of acetone, which is used extensively as a   solvent and as a starting material in the manufacture of numerous other   organic compounds";

and, in:

Acetone - Wikipedia, the free   encyclopedia; "(One) major use of acetone ... is synthesizing   bisphenol A. Bisphenol A is a component of many polymers such as   polycarbonates, polyurethanes and epoxy resins"; 

the "propanol" can be used and consumed in the synthesis of a number   of valuable plastics and polymers, which we now rely pretty much on raw   materials from OPEC to manufacture; plastics and polymers wherein the Carbon   Dioxide, consumed by the process of our subject herein, "United States Patent   Application 20120171583 - Gas Phase Electrochemical Reduction of Carbon   Dioxide", to synthesize the "propanol", would be permanently, and profitably   and productively, "sequestered".

The Carbon Dioxide recycling technology disclosed by Princeton scientist   Andrew Bocarsly, and his Princeton and Liquid Light colleagues, is similar to,   but apparently more efficient than, others, similar, we have brought to your   attention; and, one key factor seems to lie in it's "gas phase" processing.  

However, this same core team has developed other, related, CO2-recycling   processes, as well, as we will further document in reports to follow.

And, they all point to one conclusion:

Carbon Dioxide, as it arises in only a small way, relative to natural   sources of emission, such as volcanoes, from our essential use of Coal in the   generation of truly economical electric power, is a valuable raw material   resource.

As seen in the Disclosure of our subject, "United States Patent   Application 20120171583", we can efficiently convert Carbon   Dioxide into basic alcohols; and, from those alcohols, Methanol   and Propanol, we can, through other established   technologies, manufacture both various plastics and, even, Gasoline;   things we now squander our national treasure to acquire from the often   inimical nations of OPEC.

Why, in the world, would we ever want to even consider squandering   such a valuable resource as CO2 in specious scams like the mandated   geologic sequestration of CO2 in old oil wells, for the purposes of   subsidized secondary petroleum recovery?

Why, in the world, would we want to abuse the producers of such a   resource, and their customers, through  punitive Cap & Trade taxes?  

Time we all woke up, and far past time for some "good news" to be   published, ain't it?