An interconnected photosynthesis matrix and bio-energy production system. More specifically, a self-sustaining bio-system that uses the bio-energy production system, which comprises a selection process, an extraction process, and a transfer process, to create an energy enhanced organism and then uses the energy from the energy enhanced organisms for human use and/or for the second portion of the system, the photosynthesis matrix, where photosynthesis takes place. The energy is extracted from the energy enhanced organism by creating an energy rich homogenate, and then the energy is transferred to the grid, to an energy storage device, or to the photosynthesis matrix. The photosynthesis matrix consumes carbon dioxide and reduces carbon dioxide concentration while producing glucose, which it then provides to the bio-energy production system. The two systems work together in a feedback loop to allow continuous chemical reactions.

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, biofuel manufacture, and desirably impacts alternative/renewable energy production, nutrient recovery from waste streams, and valued byproducts production. The system as discussed herein is an integrated systems approach to wastewater treatment, algal strains selection for byproducts production, and recycle of algal-oil extraction waste or additional algae harvested as feedstock for 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 biofuels, fertilizer, etc. to compete with petroleum products in the marketplace.

The invention provides schemes for the integration of a fermentation process, with an electrolysis process, and a C1-generating industrial process. In particular, the invention provides process for utilizing electrolysis products, for example H.sub.2 and/or O.sub.2, to improve the process efficiency of at least one of the fermentation process or the C1-generating industrial process. More particularly, the invention provides a process whereby, H.sub.2 generated by electrolysis is used to improve the substrate efficiency for a fermentation process, and the O.sub.2 generated by the electrolysis process is used to improve the composition of the C1-containing tail gas generated by the C1-generating industrial process.

A process and system for producing a synthetic hydrocarbon having a desired H/C ratio is disclosed. Organic material is biochemically digested in a two stage biodigester for separately producing a hydrogen containing biogas substantially free of methane in a first stage and a methane containing biogas in a second stage. The methane containing biogas is reformed in a first reformer to generate hydrogen gas and carbon monoxide gas, which are then combined in a mixer with the hydrogen containing biogas into a syngas in amounts to achieve in the syngas an overall H/C ratio substantially equal to the desired H/C ratio. The syngas is reacted with a catalyst in a second reformer, a Fischer-Tropsch (FT) reactor, to produce the hydrocarbon. Using a two stage biodigester allows for the generation of separate hydrogen and methane streams, a more economical generation of the FT syngas and reduced fouling of the FT catalyst.

A system and method for producing Syngas from the CO.sub.2 in a gaseous stream, such as an exhaust stream, from a power plant or industrial plant, like a cement kiln, is disclosed. A preferred embodiment includes providing the gaseous stream to pyrolysis reactor along with a carbon source such as coke. The CO.sub.2 and carbon are heated to about 1330° C. and at about one atmosphere with reactants such as steam such that a reaction takes place that produces Syngas, carbon dioxide (CO.sub.2) and hydrogen (H.sub.2). The Syngas is then cleaned and provided to a Fischer-Tropsch synthesis reactor to produce Ethanol or Bio-catalytic synthesis reactor.

The present invention relates to improved processes and systems for purification of biological molecules, where the processes can be performed in a continuous manner.

The cell evaluation device includes a cell housing unit 111, and an adapter 120 configured to be elastically deformed by being fitted into the cell housing unit to close a top opening of the cell housing unit, and the adapter includes a body 121 to be inserted into the cell housing unit, a positioning unit 122 configured to position the body in a vertical direction with respect to the cell housing unit, a culture medium inlet port 124 and a culture medium outlet port 125 penetrating the top end and the lower end of the body, and a flexible sheet member 123 which is provided on a lower end of the body and extends radially outward from an outer edge of the lower end. This makes it possible to prevent leakage of the culture medium in the cell evaluation device.

In an illustrative embodiment, automated multi-module cell editing instruments are provided to automate multiple edits into nucleic acid sequences inside one or more cells.

The present invention relates to an anaerobic process for biogas upgrading and hydrogen utilization comprising the use of acidic waste as co-substrate. In this process, H.sub.2 and CO.sub.2 will be converted to CH.sub.4, which will result in lower CO.sub.2 content in the biogas. The invention relates to both in situ and ex situ methods of biogas upgrading. The invention further relates to a bioreactor comprising hollow fibre membranes.

A method of controlling a bioreactor system includes providing a cell culture in a bioreactor, wherein conditions in the bioreactor enable the cell culture to produce a protein of interest (POI), measuring process parameters (PPs) of the culture within the bioreactor by RAMAN, wherein the process parameters are selected from the group consisting of nutrient concentration, viable cell concentration, and protein attributes, measuring a predetermined weight of the bioreactor with the cell culture, removing cell-free spent media from the cell culture using a first output conduit at a first specified rate, removing cells from the cell culture using a second output conduit at a second specified rate, and introducing one or both of fresh media or nutrients into the cell culture using an input conduit at a third specified rate.