Abstract:
The gas-liquid reactor relates to the field of process equipment for realization of gas-liquid processes and can be used in the chemical, petrochemical and other industries. The technical result of the present invention lies in the fact that the invention provedes maximum target product output and a plug flow regime. A further technical result lies in improving convenience in using and maintaining the reactor. Another technical result lies in that the invention makes it possible to assess, during the development stage and with high accuracy, the geometrical parameters of the reactor and the effects thereof on the speed of the chemical process and the output of target product. The gas-liquid reactor comprises housing with pipes for the introduction of reagents and the removal of reaction products. The reactor housing contains a pipe bundle situated in such a way that the space between the pipes does not communicate with the internal volume of said pipes. The reactor housing is also provided with input and output pipes which communicate with the space between the pipes for the supply of a coolant or heat-carrier. A rod is removably installed in at least one of the pipes. Plates are attached to the rod, each of the plates has at least one opening. The plates are arranged in such a way that the openings of neighboring plates are not coaxial in relation to one another.
Abstract:
A reactor apparatus is provided having a reaction chamber; a compartmentalizing apparatus including a plurality of compartments, each compartment being open at a top end and bottom end, the compartmentalizing apparatus being disposed within the reaction chamber; and an inlet disposed at an area of the reactor and in fluid communication between the reaction chamber and a feed source. Also provided is a reactor apparatus having an assembly having a reaction chamber; at least one agitator assembly configured to generate mixing within the reaction chamber, the agitator assembly including: a shaft partially lined or coated with a fluoropolymer or other non-metallic corrosion-resistant material, and an impeller lined or coated with the fluoropolymer or other non-metallic corrosion-resistant material; and an inlet disposed at an area of the reactor and in fluid communication between the reaction chamber and a feed source. The provided reactor apparatus can be utilized in hydrofluorination processes.
Abstract:
A thermochemical system having a reactor or a chamber for storing a reactive material capable of absorbing a gas that is taken into the reactor by a diffuser placed along the longitudinal axis of the latter. The reactive material and the gas are such that, when placed in the presence of each other, same are subjected to a reaction causing the reactive material to absorb the gas, and conversely, same are subjected to a reaction for desorbing the gas, absorbed by the reactive material, by heating applied to the latter when it has absorbed gas. The diffuser includes a gas supply mechanism, a mechanism for dispensing the gas into the reactive material, a filtration mechanism, and a heating mechanism. The various mechanisms form a sub-assembly that is attached onto the housing of the reactor by a sealing element.
Abstract:
A high-pressure melamine reactor is provided. The high-pressure melamine reactor comprising at least one horizontal reactor body having a bottom and a top side with at least one dome integrally formed on the top side of the reactor body. The at least one horizontal reactor body comprises at least two compartments separated by at least one baffle, in particular an overflow baffle. The at least one dome is solely located above at least one of the compartments serving as melamine synthesis unit, wherein the at least one compartment serving as melamine synthesis unit comprises at least one heating element.
Abstract:
An evaporative gas generating device and a method for producing evaporative gas. A hydrogen bromide production device and a method for producing hydrogen bromide are also disclosed. The hydrogen bromide production device is provided with an evaporative gas generating device (1) that generates bromine gas, and a reactor (3) that reacts the bromine gas with hydrogen gas to form hydrogen bromide. The evaporative gas generating device (1) is provided with a container (10) that accommodates liquid bromine (B), and heating jackets (35, 36) that supply heat to a wall surface of the container (10), and heat and evaporate the liquid bromine (B) within a liquid accommodating part (15) of the container (10) to raise the temperature of the bromine gas within the evaporative gas accommodating part (16).
Abstract:
The invention discloses an ozonization continuous reaction device, comprising a raw material inlet, a raw material distributing device, one or plurality of single reaction tubes, a product outlet and an air vent. The first end of the raw material distributing device is communicated with the raw material inlet; the first end of one or plurality of single reaction tubes is communicated with the second end of the raw material distributing device; the product outlet is communicated with the second end of the single reaction tube; ozone is conveyed to the single reaction tube via the air vent. The ozonization continuous reaction device provided by the invention realizes the large-scale and continuous production of the ozonization reaction on the basis of guaranteeing security; as the single reaction tube is arranged, the ozone amount and the liquid raw material existing in the single reaction tube in unit time become fewer, the reaction security is greatly improved; in addition, the liquid raw material and the ozone are continuously fed into the reaction device, the exhaust gas and the products are continuously discharged from the reaction device, the accumulation of the ozone is prevented, the security is greatly guaranteed, and the production capacity also can be improved to a higher level.
Abstract:
A double helix gas hydrate reactor is disclosed. The reactor includes an inlet port (510) into which water and gas are supplied, an outlet port (540) disposed opposite the inlet port, a hollow jacket (580) extending from the inlet port to the outlet port, a hollow outer helix (550) installed in the hollow jacket, and an inner helix (560) installed in the outer helix. The gas and water that are supplied into the inlet port react with each other to form gas hydrate in a channel defined between the inner helix and the hollow jacket.
Abstract:
A process of treating hydrogen gas liberated from the acid or alkaline dissolution of a metal is provided. The process comprises a step of passing the liberated hydrogen gas through a reactor containing an oxidising agent for oxidation of the hydrogen gas into water, followed by a step of regenerating the oxidising agent. Also provided is an apparatus for carrying out the process, the apparatus comprising a reactor containing the oxidising agent, wherein the reactor is at least partially immersed in an alumina bath.
Abstract:
Techniques, systems and material are disclosed for transport of energy and/or materials. In one aspect a method includes generating gaseous fuel (e.g., from biomass dissociation) at a first location of a low elevation. The gaseous fuel can be self transported in a pipeline to a second location at a higher elevation than the first location by traveling from the first location to the second location without adding energy of pressure. A liquid fuel can be generated at the second location of higher elevation by reacting the gaseous fuel with at least one of a carbon donor, a nitrogen donor, and an oxygen donor harvested from industrial waste. The liquid fuel can be delivered to a third location of a lower elevation than the second location while providing pressure or kinetic energy.
Abstract:
A process of treating hydrogen gas liberated from the acid or alkaline dissolution of a metal is provided. The process comprises a step of passing the liberated hydrogen gas through a reactor containing an oxidizing agent for oxidation of the hydrogen gas into water, followed by a step of regenerating the oxidizing agent. Also provided is an apparatus for carrying out the process, the apparatus comprising a reactor containing the oxidizing agent, wherein the reactor is at least partially immersed in an alumina bath.