A process and apparatus for converting sequestered carbon to fuel, such as methane, and/or materials, such as fermentation substrates, biopolymers, bioplastics, oils, pigments, fibers, proteins, vitamins, fertilizers and animal feed. The apparatus comprises a deep well carbon-sequestering bioreactor coaxially located within a deep well anaerobic bioreactor. Carbon is sequestered into a photosynthetic biomass or a heterotrophic biomass, which is subsequently digested by an anaerobic biomass containing methanogenic microbes, whereby methane is a digestion product.

A gas stirring fermentation device has excellent mixing performance of a culture liquid and is applicable to aerobic culture requiring a high demanded oxygen amount. The gas stirring fermentation device includes a culture tank, a draft tube located inside the culture tank, and a gas supply pipe supplying gas to the inside of the culture tank, in which the gas supply pipe is provided with a gas discharge part made of a sintered metal film, and a culture liquid in the culture tank can be stirred by the gas discharged from the gas discharge part.

The invention relates to a digester for a liquid medium, comprising a container, a dividing wall between two spaces, and a device for injecting gas into the lower part of one of the spaces. The gas creates an upflow of the mixture of liquid medium and injected gas in said space, and a downflow in the other space. The dividing wall is equipped with at least one device for establishing a fluid communication between the spaces, so that the fluid communication configuration is automatically varied between a first open configuration in which fluid can flow freely from one space to the other, and a second closed configuration in which the flow of fluid is blocked fully or partially by the aforementioned device.

The present invention relates to a reaction device with air-lift type internal circulation which includes:a vertical cylindrical volume;a vertical element positioned within said volume in such a way as to form an interspace with the walls of said volume, having a cross-section which is circular and orthogonal to the vertical axis of the element and with a variable internal diameter along said axis, said element being denoted draft tube;at least one gas distributor positioned on the bottom of said device; said device being characterised in that:the ratio between the diameter of the internal vertical element and the internal diameter of the cylindrical volume ranges from 0.05 to 0.5, andthe ratio between the height of the vertical element and the height of the cylindrical volume is less than 0.5.

A membrane fibre bunch for use in a membrane-aerated biofilm reactor (MABR), the membrane fibre bunch comprising: a group of membrane fibres arranged as a bunch (4) of vertical or horizontal membrane fibres attached at either end to an gas supply manifold (8) within the housing, with each fibre having a lumen containing a gas phase; and a means for connecting the group of membrane fibres so that the gas can flow within the lumen of the membrane; wherein the group of membrane fibres are maintained in position by a connector or overmold (10), the connector or overmold configured to maintain the group of membrane fibres (2) in a spaced-apart configuration from one another and the cross-section of the connector/overmold being of non-circular shape such as ellipsoidal, star-shape etc.

The present invention discloses an airlift reactor assembly with a helical sieve plate, comprising a reaction tank, wherein a draft tube and a gas sparger are assembled in the reaction tank, the gas sparger is arranged just below an riser section of the draft tube, a helical sieve plate is arranged in the riser section of the draft tube, and a body of the helical sieve plate is helical upwards to guide a part of two/three-phase flow in the riser section, and the body of the helical sieve plate is provided with a plurality of sieve meshes to guide the remaining two/three-phase go through the helical sieve plate in the riser section and to break bubbles. The present invention gives consideration to both macroscopic mixing and microscopic mixing processes. In addition to driving liquid to circularly flow by using ejected gas, the helical sieve plate can be used for breaking large bubbles into small bubbles thereby effectively preventing the bubbles from coalescing, increasing gas holdup and increasing a volumetric oxygen transfer coefficient.

According to embodiments of the present invention, a bioreactor for growing photoautotrophic organisms is provided. The bioreactor includes a vessel configured to receive the photoautotrophic organisms, the vessel having a longitudinal axis, which a circumferential wall extends around said axis, wherein said circumferential wall is translucent so as to enable light to enter the vessel from the outside for acting on the photoautotrophic organisms, wherein a device for providing an uneven distribution of the light intensity within said vessel along said axis is provided.

The present invention relates to a process for production of fermentation products, including bioethanol by non-pressurized pre-treatment, enzymatic hydrolysis and fermentation of waste fractions containing mono- and/or polysaccharides, having a relatively high dry matter content. The process in its entirety, i.e. from non-pressurized pre-treatment over enzymatic hydrolysis and fermentation to sorting of fermentable and non-fermentable solids can be processed at a relatively high dry matter content in a single vessel or similar device using free fall mixing for the mechanical processing of the waste fraction.

This disclosure describes a biochemical reactor with a lower divider support structure. The biochemical reactor may include a tank configured to house immobilized carriers and fluid. The biochemical reactor may include a circulation conduit at least partially disposed within the tank. The circulation conduit may include a circulation outlet opening. The biochemical reactor may include one or more vanes disposed proximate to the circulation outlet opening. The biochemical reactor may include a tank recirculation port disposed proximate to a second end. The biochemical reactor may include a tank inlet configured for feeding fluid into the tank. The biochemical reactor may include a tank outlet configured for drawing fluid from the tank. The tank outlet may be disposed proximate to a first end. The biochemical reactor may include a first divider and a second divider. The second divider may include a support structure including a grating configured to withstand variable loads.

A bioreactor for growing micro-organisms, has a reaction chamber containing a reaction mixture with a reaction medium and micro-organisms. A draft tube is arranged inside the reaction chamber, which has a gas inlet, an inlet for the reaction mixture at its first end, and an outlet for the reaction mixture at its second end. The bioreactor includes means for generating flow of the reaction mixture within the reaction chamber and a first blade structure arranged inside the reaction chamber, surrounding the draft tube. The first blade structure has blades arranged at, at least one of an angle .sub.1 with respect to a direction defined by the height of the reaction chamber, or an angle .sub.2 with respect to a direction defined by the height of the reaction chamber. The bioreactor also includes an inlet for reaction medium and an outlet for withdrawing medium with grown micro-organisms.