C12M43/00

Methods and systems for the production of alcohols and/or acids
11618910 · 2023-04-04 · ·

Methods and systems for the production of one or more products from a gas stream produced in a methanol production process. The method comprises converting at least a portion of a methane feedstock to a substrate comprising CO and H2. The substrate comprising CO and H2 is anaerobically fermented in a bioreactor to produce one or more alcohols. The method and system may further include process for the production of methanol processes for the production of acetic acid.

Chemical Reformer Systems And Methods
20220314192 · 2022-10-06 ·

A chemical reformer system has an inlet, a digester, a series of chemical reformers, coolers and separators. The temperatures and pressures of the digester and chemical reformers may be regulated, where the pressure decreases from the first chemical reformer to the last and the temperature increases from the first chemical reformer to the last. The chemical reformer system may be utilized to convert feedstock biomass to output compounds, such as bio-oils.

FOOD WASTE DIGESTER
20230151321 · 2023-05-18 · ·

A method of processing food waste in a food waste digester using processed tagua seeds as a support medium for micro-organism that digest food waste into a biodegradable liquid.

METHOD AND SYSTEM FOR PRODUCING A CARBONATE-CONTAINING SPECIES-RICH, NITROGEN-CONTAINING SPECIES-FREE SOLUTION

A method for producing a carbonate-containing species-rich, nitrogen-containing species-free solution from a urea-rich solution is proposed. The method comprising the steps of: providing a first reservoir comprising a first mixture including urea and a catalyser comprising an enzymatic catalyser and/or a microorganism; allowing an enzymatic reaction catalysed by the catalyser to decompose urea, thereby obtaining a second mixture comprising nitrogen-containing species and carbonate-containing species; converting at least some of the nitrogen-containing species into gaseous nitrogen-containing species to obtain a third mixture comprising the gaseous nitrogen-containing species and the carbonate-containing species; filtering the third mixture by a gas- permeable filter, thereby separating at least some of the gaseous nitrogen-containing species from the carbonate-containing species while keeping the catalyser away from the gas-permeable filter; and collecting the so-obtained carbonate-containing species-rich, nitrogen-containing species-free solution.

SYSTEMS AND METHODS FOR TREATING WASTE STREAMS
20230203414 · 2023-06-29 ·

According to present disclosure, there is disclosed an algae growth and cultivation system that provides a cost-efficient means of producing algae biomass as feedstock for algae-based products, such as, fertilizer, feed, biofuel manufacture, and desirably impacts, nutrient recovery from waste streams for valued byproducts production, recycle water, and alternative/renewable energy production. The system as discussed herein is an integrated systems approach to wastewater treatment, algal strains selection for byproducts production, and recycle of algal biomass-processing waste or additional algae harvested as feedstock for products such as fertilizer production. Embodiments of a system as discussed herein present an economically viable algae production system and process that allows algae-derived products such as fertilizer, feed, biofuels, etc. to compete with non-organic or petroleum products in the marketplace.

Variable Diameter Bioreactors
20170369828 · 2017-12-28 ·

A variable diameter bioreactor vessel is provided that includes a first vessel section having a first diameter configured to hold a liquid media and biologic material, and a second vessel section having a second diameter that is greater than the first diameter such that the liquid media can be increased from a first volume to a second volume within the vessel.

SYSTEM AND METHOD FOR CARBON DIOXIDE REACTOR CONTROL

A system optionally including a carbon oxide reactor. A method for carbon oxide reactor control, optionally including selecting carbon oxide reactor aspects based on a desired output composition, running a carbon oxide reactor under controlled process conditions to produce a desired output composition, and/or altering the process conditions to alter the output composition.

Variable Diameter Bioreactors
20230183623 · 2023-06-15 ·

A variable diameter bioreactor vessel is provided that includes a first vessel section having a first diameter configured to hold a liquid media and biologic material, and a second vessel section having a second diameter that is greater than the first diameter such that the liquid media can be increased from a first volume to a second volume within the vessel.

Production System and Method of Production for Organic Compound or Microorganism

Provided is a novel production system that does not involve, or can minimize, the transport of liquid ammonia in the production of an organic compound or the production of a microorganism by microbial fermentation. A production system for an organic compound or a microorganism includes: an ammonia synthesis apparatus in which an ammonia-containing gas is synthesized by reaction of a source gas containing hydrogen and nitrogen in the presence of a supported ruthenium catalyst; and a culture apparatus that cultures a microorganism having organic compound productivity using ammonia originating from the ammonia-containing gas obtained by using the ammonia synthesis apparatus.

ARRANGEMENT FOR THE CULTIVATION AND UTILIZATION OF BIOMASS AND SYSTEM OF ARRANGEMENTS FOR THE CULTIVATION AND UTILIZATION OF BIOMASS
20230167390 · 2023-06-01 ·

An arrangement (1) for the cultivation of plants and for the utilization of biomass waste and a system (1000) of at least one arrangement (1) for the cultivation and utilization of biomass are disclosed. The arrangement (1) comprises a modular greenhouse (100) and a modular, two-stage biogas plant (200). The system (1000) has at least one arrangement (1) wherein a control and monitoring unit (101) of the modular greenhouse (100) and a further a control and monitoring unit (201) of the two-stage biogas plant (200) are communicatively connected to a central control and monitoring unit (55).