Embodiments disclosed herein relate to the production of polypropylene. At least one olefin monomer stream (10, 12) is fed to a polymerization zone (2). A recirculation gas stream (31) is withdrawn therefrom, compressed into a compressor (4), cooled in a first heat exchanger (5), separated in a phase separator (6), flashed in a pressure regulator (7), fed to a second heat exchanger (8), and recycled (83) to the polymerization zone (2).

A green hydrogen production system, a green power production system, a green hydrogen and green power production system, and methods of implementing the same are provided. Catalyst for hydrogen production is sent to a raw-material mixing unit, mixed with water, and then reacted in a first water splitting unit therein to generate hydrogen gas and oxidized catalyst for hydrogen production. The hydrogen gas is delivered to a hydrogen power generation unit to produce power while the oxidized catalyst for hydrogen production is sent to a photon-plasma decomposition unit for being reduced into the catalyst for hydrogen production and oxygen generated is sent to the hydrogen power generation unit to generate power. Thereby hydrogen, power, and raw materials used in the system are recycled during operation. Therefore, green hydrogen and green power with reasonable price obtained can replace fossil fuels to solve climate change and global warming issues.

A process for preparing metal chloride Mx+Clx, in which metal carbonate in solid form is reacted with a chlorinating agent selected from chlorine and oxalyl chloride to give metal chloride Mx+Clx, where the metal M is selected from the group of the alkali metals, alkaline earth metals, Al and Zn, Li and Mg, or Li, and x corresponds to the valency of the metal cation, and wherein metal M is additionally added as a reactant to the metal carbonate/chlorinating agent reaction.

An apparatus and method sinters or partially sinters green pellets in a selected temperature range to make proppant particles as the green pellets pass through a first central portion of the first vortex gas flow and exit the second end of the first cylindrical vessel and/or pass through a second central portion of the second vortex flow and exit the fourth end of the second cylindrical vessel.

The present disclosure relates to a device and process for preparing sebacic acid through electromagnetic induction heating coupled with dry constant-temperature alkaline hydrolysis. The device includes an electromagnetic heating cylinder and a reaction kettle arranged in the electromagnetic heating cylinder, heat storage pellets fill space between the reaction kettle and the electromagnetic heating cylinder, and the heat storage pellets adhere to an inner wall of the electromagnetic heating cylinder and an outer wall of the reaction kettle. The upper end of the reaction kettle is provided with a feeding port, a gas outlet and a temperature measuring port, the reaction kettle is also provided with a stirring device, a lower portion of the reaction kettle is provided with a discharging port, and the feeding port, the gas outlet, the temperature measuring port and the discharging port all extend out of the thermal insulation cotton.

The present invention relates generally to utilizing gasses for fragmenting polymeric materials and simultaneously modifying the surface area molecular structure of the said polymeric materials. More particularly, the present invention relates to a method and associated device for the processing of already preliminarily deformed polymeric materials, preferably without metal reinforcing elements, by utilizing aggressive gasses to both modify the polymeric materials surface area into an activated state and also simultaneously fragment the fed preliminarily deformed polymeric materials into a powder-like form with a relatively increased surface area.

The invention relates to a system for the continuous polymerization of -olefin monomers comprising a reactor, a compressor, a cooling unit and an external pipe, wherein the reactor comprises a first outlet for a top recycle stream, wherein the system comprises apparatus, wherein the reactor comprises a first inlet for receiving a bottom recycle stream, wherein the reactor comprises an integral separator, wherein the first inlet of the integral separator is connected to a first outlet, wherein the first outlet for the liquid phase is connected to the second outlet of the reactor for the liquid phase, wherein the external pipe comprises a second inlet for receiving a solid polymerization catalyst, wherein the first outlet of the external pipe is connected to a second inlet of the reactor, wherein the reactor comprises a third outlet, wherein the system comprises a first inlet for receiving a feed.

A method for producing metal chloride M.sup.x+Clx includes reacting metal carbonate in solid form using phosgene, diphosgene and/or triphosgene to form metal chloride M.sup.x+Clx, wherein the metal M is selected from the group containing alkali metals, alkaline earth metals, Al and Zn, Li and Mg, or Li, for example, and x corresponds to the valency of the metal cations. An apparatus for performing such method is also disclosed.

A reactor system may comprise a moving bed reactor, a fluidized bed reactor, and a separation unit. The moving bed reactor may comprise catalyst material particles comprising a metal oxide support and a transition metal alloy, where the transition metal alloy comprises two transition metal elements. The moving bed reactor may comprise an inlet configured to receive a hydrocarbon and an outlet configured to provide hydrogen (H2) generated within the moving bed reactor. The fluidized bed reactor may be in fluid communication with the moving bed reactor and configured to receive the catalyst material particles and deposited carbon material from the moving bed reactor. The separation unit may be in fluid communication with an outlet of the fluidized bed reactor and configured to separate the catalyst material particles from carbon material and inert gas. The separation unit may be in fluid communication with the moving bed reactor.

The present disclosure generally relates to a liquid-solid radial moving bed reaction apparatus comprising a radial moving bed reactor, a spent catalyst receiver, a catalyst regenerator, and a regenerated catalyst receiver that are successively connected. Also disclosed is a solid acid alkylation process using the liquid-solid radial moving bed reaction apparatus.