Provided herein are methods, devices and systems for processing of carbonaceous compositions. The processing may include the manufacture (or synthesis) of oxidized forms of carbonaceous compositions and/or the manufacture (or synthesis) of reduced forms of oxidized carbonaceous compositions. Some embodiments provide methods, devices and systems for the manufacture (or synthesis) of graphite oxide from graphite and/or for the manufacture (or synthesis) of reduced graphite oxide from graphite oxide.

Provided herein are methods, devices and systems for processing of carbonaceous compositions. The processing may include the manufacture (or synthesis) of oxidized forms of carbonaceous compositions and/or the manufacture (or synthesis) of reduced forms of oxidized carbonaceous compositions. Some embodiments provide methods, devices and systems for the manufacture (or synthesis) of graphite oxide from graphite and/or for the manufacture (or synthesis) of reduced graphite oxide from graphite oxide.

Provided herein are methods, devices and systems for processing of carbonaceous compositions. The processing may include the manufacture (or synthesis) of oxidized forms of carbonaceous compositions and/or the manufacture (or synthesis) of reduced forms of oxidized carbonaceous compositions. Some embodiments provide methods, devices and systems for the manufacture (or synthesis) of graphite oxide from graphite and/or for the manufacture (or synthesis) of reduced graphite oxide from graphite oxide.

The invention refers to a flow-promoting device (100; 100; 100″) for performing a biological or chemical transformation, or physical or chemical trapping from, or release of agents to, a fluidic medium. The flow-promoting device (100; 100; 100″) comprises a ferromagnetic material (5) and a retaining structure (1; 1; 1″), the retaining structure having a compartment (9; 9″) defined by a permeable material (11; 11″). The retaining structure (1; 1; 1″) comprises a top wall (3; 3″) and a circumferential side wall (4; 4″), wherein the top wall (3; 3″) and the circumferential side wall (4; 4″) is formed mainly by said permeable material (11; 11″). The compartment (9; 9″) of the retaining structure (1; 1; 1″) is arranged to contain at least one fluid-permeable solid reaction member.

The invention refers to a flow-promoting device (100; 100; 100″) for performing a biological or chemical transformation, or physical or chemical trapping from, or release of agents to, a fluidic medium. The flow-promoting device (100; 100; 100″) comprises a ferromagnetic material (5) and a retaining structure (1; 1; 1″), the retaining structure having a compartment (9; 9″) defined by a permeable material (11; 11″). The retaining structure (1; 1; 1″) comprises a top wall (3; 3″) and a circumferential side wall (4; 4″), wherein the top wall (3; 3″) and the circumferential side wall (4; 4″) is formed mainly by said permeable material (11; 11″). The compartment (9; 9″) of the retaining structure (1; 1; 1″) is arranged to contain at least one fluid-permeable solid reaction member.

The invention relates to a system for processing liquid and/or solid compounds, comprising a vessel (3) and a holding device (5) for the vessel (3), the holding device (5) comprising a stop (15) against which the vessel (3) rests after being inserted into the holding device (5) and a supply unit (7) opposite the stop (15), the supply unit (7) comprising a closing element (9), which can be set to a first and a second position, wherein in the first position of the closing element (9) the vessel (3) can be inserted into the holding device (5) and in the second position of the closing element (9) the vessel (3) inserted into the holding device (5) is pressed against the stop (15) by the closing element (9).

The invention relates to a system for processing liquid and/or solid compounds, comprising a vessel (3) and a holding device (5) for the vessel (3), the holding device (5) comprising a stop (15) against which the vessel (3) rests after being inserted into the holding device (5) and a supply unit (7) opposite the stop (15), the supply unit (7) comprising a closing element (9), which can be set to a first and a second position, wherein in the first position of the closing element (9) the vessel (3) can be inserted into the holding device (5) and in the second position of the closing element (9) the vessel (3) inserted into the holding device (5) is pressed against the stop (15) by the closing element (9).

Chemical reactor with high speed rotary mixing, system thereof, and method thereof, for catalytic thermal conversion of organic (hydrocarbon-containing) materials (coal, plastics, rubber, plant matter, wood shavings, biomass, organic wastes) into diesel and other liquid fuels (automobile or/and jet engine fuels). Relevant to non-conventional commercial scale production of liquid fuels, and to commercial scale processing and disposing of organic waste materials. Chemical reactor includes: integrated combination of a reactor stationary assembly (RSA), having only stationary components remaining stationary during chemical reactor operation, and a reactor rotary mixing assembly (RRMA), having only rotatable components rotating during chemical reactor operation. May include anti-abrasion shield for shielding inner surface of reactor central housing from abrasion during chemical reactor operation. Rotor may include a reinforcement disc. Rotor blades or/and reinforcement disc may include rotor-based performance and process control structural features (openings, or/and protrusions, or/and depressions), for additionally controlling performance of the rotor.

The present application relates to an olefin polymerization method and system in the field of olefin polymerization. The method combines a supported double catalyst with a series process, introduces a liquid material obtained after heat exchange and gas-liquid separation of a circulation gas flow into a separate first reactor to get into contact with the supported double catalyst for polymerization reaction, and then introduces the reaction material and the first polyolefin generated by reaction into a second reactor to continue polymerization reaction, thereby enabling particles to circulate between first reactor and second reactor, improving mixing effect of two polyolefins with obvious differences in properties, avoiding the occurrence of phase separation, and facilitating the production of polyolefins with excellent performance. At the same time, ethylene gas is introduced into first reactor to further reduce the hydrogen/ethylene ratio, increase the molecular weight of polyethylene and improve the product performance.

A continuous slurry-bed tank reactor, comprising a tank reactor body, an agitator, and tubular separation membranes. A method of using the continuous slurry-bed tank reactor comprising adding a catalyst, feeding reactants, stopping feeding the reactants, starting a heating system, changing directions of the reactants flowing through the tubular separation membranes.