Methods for optimizing gas utilization

US2023398487A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2023398487-A1
Application numberUS-202318455342-A
CountryUS
Kind codeA1
Filing dateAug 24, 2023
Priority dateJul 11, 2019
Publication dateDec 14, 2023
Grant date

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

Official abstract text for this publication.

The invention provides for the optimal utilization of gas by a fermentation process, whereby the various components within the gas stream are separated to increase the efficiency of the microorganisms. The invention is capable of tailoring the composition of the gas being used by the fermentation process so as to enhance the production of various products. The invention is capable of applying such controlled separation and utilization of gas to produce different products in two fermentation processes in series. The invention is also capable of applying such controlled separation and utilization of gas to produce one product in a first fermentation process, which may be converted to a different product in a second fermentation process. The invention is additionally capable of mitigating culture inhibition.

First claim

Opening claim text (preview).

1 . A method for optimizing the flow of gas to fermentation processes in series, the method comprising: a. separating a gas stream derived from at least one industrial source into a hydrogen rich stream and a hydrogen depleted stream using at least one hydrogen separation module; b. fermenting at least a portion of the hydrogen rich stream in a first fermentation process using at least one reactor comprising a liquid nutrient medium containing a culture of one or more C1-fixing microorganism to produce a first fermentation product; and c. fermenting at least a portion of the hydrogen depleted stream in a second fermentation process comprising at least one reactor comprising a liquid nutrient medium containing a culture of one or more C1-fixing microorganism to produce a second fermentation product, wherein at least a portion of the first fermentation product is passed to the second fermentation process; and wherein the hydrogen rich stream comprises H 2 and CO at a H 2 to CO ratio from 2:1 to 5:1 and the hydrogen depleted stream comprises H 2 and CO at a H 2 to CO ratio from 0.05:1 to less than 2:1. 2 . The method of claim 1 , wherein the first fermentation product is acetic acid. 3 . The method of claim 2 , wherein at least a portion of the acetic acid from the first fermentation process is converted to ethanol in the second fermentation process. 4 . The method of claim 1 , wherein the hydrogen separation module is a pressure swing adsorption process. 5 . The method of claim 1 , wherein the industrial source is selected from the group consisting of carbohydrate fermentation, gas fermentation, cement making, pulp and paper making, steel making, oil refining and associated processes, petrochemical production, coke production, anaerobic or aerobic digestion, gasification, natural gas extraction, methane reformation, oil extraction, metallurgical processes, for production and/or refinement of aluminium, copper, and/or ferroalloys, geological reservoirs, and catalytic processes. 6 . The method of claim 1 , wherein at least a portion of the gas stream is comprised of a blast furnace top gas from a metallurgical process. 7 . The method of claim 1 , wherein at least a portion of a vent gas produced in the first fermentation process is recycled to the hydrogen rich stream. 8 . The method of claim 7 , wherein at least a portion of the vent gas produced in the first fermentation process is passed through a pressure swing adsorption process prior to being recycled to the hydrogen rich stream. 9 . The method of claim 1 , wherein at least a portion of a vent gas produced in the second fermentation process is recycled to the hydrogen depleted stream. 10 . The method of claim 9 , wherein at least a portion of the vent gas produced in the second fermentation process is passed through a pressure swing adsorption process prior to being recycled to the hydrogen depleted stream. 11 . The method of claim 1 , wherein the C1-fixing microorganism is selected from the group consisting of Moorella, Clostridium, Ruminococcus, Acetobacterium, Eubacterium, Butyribacterium, Oxobacter, Methanosarcina , and Desulfotomaculum. 12 . The method of claim 1 , wherein the C1-fixing microorganism is Clostridium autoethanogenum. 13 . A method for optimizing gas flow to a fermentation process, the method comprising: a. fermenting at least a portion of a gas stream from an industrial source using at least one reactor comprising a liquid nutrient medium containing a culture of one or more C1-fixing microorganism to produce a fermentation product and a vent gas stream; and b. recycling at least a portion of the vent gas stream to the bioreactor, wherein the recycling of at least a portion of the vent gas stream to the bioreactor reduces and/or mitigates the potential inhibition of the culture. 14 . The method of claim 13 , wherein at least a portion of the vent gas is passed through a pressure swing adsorption process prior to being recycled to the bioreactor. 15 . The method of claim 14 , wherein the pressure swing adsorption process removes at least a portion of at least one component selected from the group consisting of carbon dioxide, inorganic hydrocarbons, tars, organic nitrogen, and organic and inorganic sulfur from the vent gas stream. 16 . The method of claim 14 , wherein the pressure swing adsorption process simultaneously removes at least a portion of at least two components selected from the group consisting of carbon dioxide, inorganic hydrocarbons, tars, organic nitrogen, and organic and inorganic sulfur from the vent gas stream.

Assignees

Inventors

Classifications

  • Biological processes · CPC title

  • Acetic acid (vinegar C12J) · CPC title

  • B01D53/047Primary

    Pressure swing adsorption · CPC title

  • C12P7/065Primary

    with microorganisms other than yeasts · CPC title

  • C12P7/14Primary

    Multiple stages of fermentation; Multiple types of microorganisms or re-use of microorganisms · CPC title

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US2023398487A1 cover?
The invention provides for the optimal utilization of gas by a fermentation process, whereby the various components within the gas stream are separated to increase the efficiency of the microorganisms. The invention is capable of tailoring the composition of the gas being used by the fermentation process so as to enhance the production of various products. The invention is capable of applying s…
Who is the assignee on this patent?
Lanzatech Inc
What technology area does this patent fall under?
Primary CPC classification B01D53/047. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Thu Dec 14 2023 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).