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200results about How to "Increase operating pressure" patented technology

Multi-effect rectifying process of methanol

The invention relates to a multi-effect rectifying process of methanol, which belongs to the technical field of separation and purification of chemical products. In the process, a crude methanol raw material of coal-to-methanol is rectified by a pre-rectifying tower, a pressurizing tower I, a pressurizing tower II, an atmospheric tower and a recovery tower in turn at appropriate temperature and pressure so as to obtain a high-purity refined methanol product according with quality requirements. In the flow, methanol steam on the top of the pressurizing tower I is used for providing heat for a reboiler at the bottom of the pressurizing tower II, the methanol steam on the top of the pressurizing tower II is used for providing heat for a reboiler at the bottom of the atmospheric tower, and the pressurizing tower I, the pressurizing tower II and the atmospheric tower form multi-effect rectification; and simultaneously, the methanol steam on the top of the recovery tower is used for providing heat for a reboiler at the bottom of the pre-rectifying tower, and the recovery tower and the pre-rectifying tower form double-effect rectification. The invention provides an energy-saving methanol multi-effect rectifying process method which has the advantages of greatly reduced energy consumption, more stable production process, more easily controlled product quality, higher methanol recovery rate and basically equivalent investment compared with a three-tower rectifying process.
Owner:XI'AN PETROLEUM UNIVERSITY

IGCC (Integrated Gasification Combined Cycle) poly-generation device and method based on pyrolysis and gasification of low metamorphic powdered coal

The invention discloses an IGCC (Integrated Gasification Combined Cycle) poly-generation device and method based on pyrolysis and gasification of low metamorphic powdered coal. The device comprises a pyrolysis/gasification system, a coal gas purifying system, a circulating fluidized bed boiler and a gas turbine/steam turbine system. The method comprises the steps as follows: carrying out low temperature pyrolysis and partial air gasification on the low metamorphic powdered coal, grading and converting into coal gas, tar and semi-coke, and carrying out the IGCC poly-generation process by the semi-coke and the coal gas with high calorific value. According to the device and the method, the tar, sulphur and other chemical products can be produced while clean power is generated, the products obtained by grading and converting the low metamorphic powdered coal are fully utilized, the material conversion and energy conversion functions are integrated, the resource utilization rate is high, and the heat energy efficiency is high. The device and method are suitable for the low metamorphic powdered coal such as peat, brown coal, jet coal, non-sticking coal and the like, and the particle size of raw materials is 0-8 mm. The high-temperature coal gas generated in a fluidized bed gasification furnace contains a large amount of hydrogen, so that the powdered coal can be subjected to hydropyrolysis, and the tar recovery rate can reach more than 12%.
Owner:陕西华祥能源科技集团有限公司

Circulated coal gas heat carrier fluidized bed ash coal pyrolysis device and method

The invention discloses a circulated coal gas heat carrier fluidized bed ash coal pyrolysis device and method. The device comprises a coal-adding system and a fluidized bed pyrolyzing furnace which is communicated with the coal-adding system and provided with a coke-discharging hole, wherein the gas distributor of the fluidized bed pyrolyzing furnace is communicated with a high temperature heating furnace, the coal gas outlet of the fluidized bed pyrolyzing furnace is communicated with a first-stage cyclone separator, a second-stage cyclone separator, a high temperature deep dust collector and a gas cooler in turn through a pipeline, the lower outlet of the gas cooler is communicated with a separator, and the gas outlet of the gas cooler is connected with the high temperature heating furnace and a coal gas delivering device respectively. The device has simple flow and does not require an air separation device; as the circulated coal gas contains a lot of hydrogen, the hydropyrolysis of coal is realized to a certain extent, the yield of oil is increased to above 12%; and the operating pressure can be increased to the medium/high level, and industrial clusters and polygeneration are applied on the basis of equipment scale expansion while the products such as coal gas with high calorific value, semicoke, tar and the like are prepared.
Owner:陕西华祥能源科技集团有限公司

Method for depriving solvent for cis-polybutadiene

The invention relates to a method for depriving a solvent for cis-polybutadiene, which is mainly used for solving the problems of high consumption of solvent naphtha and large consumption of water vapor in the prior art. The technical scheme adopted by the invention comprises the following steps: a) injecting a material stream I containing rubber liquid cement and hot water from the upper part ofa first cohesion kettle, ejecting a material stream II containing water and solvent from the top of the first cohesion kettle, and ejecting a material stream III from an overflow pipe at the lateral part of the first cohesion kettle, wherein the flow capacity of the material stream III is controlled by a liquid level controlling system; b) feeding the material stream III from a gas phase spatial position in the second cohesion kettle, after the material stream containing water and solvent is drawn out by vacuum-pumping equipment, feeding the material stream containing water and solvent into the bottom of the first cohesion kettle together with the supplementary fresh steam, and carrying out cohesion, thus obtaining a material containing cis-polybutadiene at the bottom of the second cohesion kettle; and c) obtaining the solvent after the stream II containing water and solvent is subjected to separation. By utilizing the technical scheme provided by the invention, the problems in the prior art can be better solved; and the method for deprivating the solvent for cis-polybutadiene can be applicable to the industrial production for deprivating the solvent for the cis polybutadiene.
Owner:CHINA PETROLEUM & CHEM CORP

Energy-saving water-saving organic silicon monomer rectifying method

The invention discloses an energy-saving water-saving organic silicon monomer rectifying method which adopts a cis cleavage multi-tower flow. In the rectifying method, the tower top material steam of a high-boiling component removing tower firstly enters a main distribution manifold, then heat is respectively supplied for tower bottom reboilers of a low-boiling component removing tower, a light component removing tower, a hydrogenous tower, an azeotropic tower, a trimethylchlorosilane separating tower, a methyl trichloro silicane separating tower and a dimethyldichlorosilane separating tower through the main distribution manifold, the tower top material steam of the high-boiling component removing tower after heat supply is condensed into liquid, is then cooled to the reflux temperature through an air cooler and enters a tower top reflux tank of the high-boiling component removing tower, a second reboiler is connected with the tower bottom of the dimethyldichlorosilane separating tower, and vapor is adopted for the heat exchange of the reboiler. By adopting the method, because the operating pressure and the operating temperature of the high-boiling component removing tower and the methyl trichloro silicane separating tower with larger cooling quantity requirements are increased, at least two towers in the flow have the condition of adopting air cooling, thereby reducing the circulating water quantity and decreasing the evaporation loss; and the energy-saving water-saving organic silicon monomer rectifying method has strong operation controllability, flexible mode, multiple control means, smaller pressure increasing amplitude and high operation security.
Owner:TIANJIN UNIV

Carbon fiber reinforced plastic electric-smelting pipe fitting with strain self-monitoring function

The invention relates to the field of thermoplastic plastic electric-smelting pipe fittings, and aims to provide a carbon fiber reinforced plastic electric-smelting pipe fitting with the strain self-monitoring function. The carbon fiber reinforced plastic electric-smelting pipe fitting comprises an electric-smelting pipe fitting body with a resistor wire buried, and two binding posts respectivelyconnected to the two ends of the resistor wire are arranged on the electric-smelting pipe fitting body. The carbon fiber reinforced plastic electric-smelting pipe fitting is characterized in that theelectric-smelting pipe fitting body is made of thermoplastic plastic filled with the carbon fiber, at least one set of paired electrodes is arranged on the surface of the electric-smelting pipe fitting body and used for monitoring the changes of the resistance values due to thermal temperature rising or internal pressure deformation in the suing process so as to achieve the strain monitoring of the electric-smelting pipe fitting. The carbon fiber reinforced plastic electric-smelting pipe fitting can improve the elastic modulus and yield strength of the material, has higher mechanical strength,higher blasting pressure, and can improve the operating pressure, the strain of the electric-smelting pipe fitting and the pressure inside the electric-smelting pipe fitting can be monitored, the additional equipment does not need, the intelligence and safety of the electric-smelting pipe fitting are improved, and the manufacturing process is simple, the stability is high, and the cost of the process is reduced.
Owner:ZHEJIANG UNIV

Method and system for producing ethyl chloride

The invention discloses a method for producing ethyl chloride, which comprises steps as follows: hydrochloric acid and zinc chloride after concentration by evaporation enter a hydrochloric acid heating unit from the bottom to be heated, enter an ethyl chloride reactor, and are subjected to thermal separation of the ethyl chloride and mixed solution; the separated magnesium chloride enters an evaporation dehydrator to be heated; the zinc chloride solution is concentrated; and the high-concentration zinc chloride naturally flows to the lower part of a hydrochloric acid evaporator to be recycled. The invention can be matched with a climbing film graphite evaporator with larger heat transfer area to implement the large-size ethyl chloride reactor and enhance the level of the ethyl chloride industrialization device; the reaction rate and raw material conversion rate are enhanced; graphite is used as the distributor of the ethyl chloride reaction part, so the corrosion resistance is high; the steel liner polytetrafluoroethylene cylinder and pipeline are adopted, thereby resisting corrosion and enhancing the operating pressure and equipment utilization ratio; and in addition, the invention is convenient to operate, enhances the production efficiency of ethyl chloride, and has favorable application value.
Owner:JIANGSU YINZHU CHEM GROUP

Optimum process for selective hydrogenation/hydro-isomerization, aromatic saturation, gasoline, kerosene and diesel/distillate desulfurization (HDS). RHT-hydrogenationSM, RHT-HDSSM

A process for selective hydrogenation of C3 / C4 / C5 / C6 / C7 and LCN, hydro-isomerization of olefins, benzene saturation and hydrodesulfurization of Gasoline, Kerosene and Diesel together with aromatic saturation of LCO is being provided so as to provide optimum technology at low cost with unique configuration. The technology is user friendly and uses conventional catalyst. These configurations cover both the options of installing the bulk catalyst in the distillation column with chimneys trays, hence essentially all the reaction takes place in the liquid phase in single or multiple beds or with fixed bed down flow or up flow reactor configuration. The configurations shown in the figures depicts that the fixed bed reactors are integrated with the Distillation Column and this art helps in lowering the Capital costs and the reactors are operating in single phase or two-phase conditions. The art is applicable to MAPD, vinyl acetylene, C3, C4, C5, C6, C7 mixed hydrocarbon stream, and LCN diolefin selective hydrogenation. It includes the process for hydro-isomerization of Butene-2 to Butene-1, or visa versa, removal of Isobutylene and Isobutane by distillation after hydro isomerization, benzene hydrogenation to Cyclohexane, hydrodesulfurization of FCC gasoline, coker gasoline or any other Naphtha stream together with hydrodesulfurization of Diesel / Kerosene from any of the refinery units.
Owner:REFINING HYDROCARBON TECH RHT

Pressure-enhanced, adaptive inflator device

An inflator device that includes a diffuser chamber with a first combustion chamber and a second combustion chamber each connected to the diffuser chamber. A supply of a first gas-generating pyrotechnic material having a burn rate that is pressure dependent is contained within the first combustion chamber. The first combustion chamber forms or includes an orifice providing independent fluidic communication between the first combustion chamber and the diffuser chamber. This orifice throttles a single stage combustion wherein the supply of the first gas-generating pyrotechnic material is selectively reactable to produce a first combustion chamber single stage combustion product gas. A supply of a second gas-generating pyrotechnic material is contained within the second combustion chamber. The second combustion chamber forms or includes an orifice that provides independent fluidic communication between the second combustion chamber and the diffuser chamber. This orifice throttles a single stage combustion wherein the supply of the second gas-generating pyrotechnic material is selectively reactable to produce a second combustion chamber single stage combustion product gas. The diffuser chamber forms or includes at least one exit orifice. This diffuser exit orifice throttles a dual stage combustion wherein the supply of the first gas-generating pyrotechnic material is reactable to produce a first combustion chamber dual stage combustion product gas and the supply of the second gas-generating pyrotechnic material is reactable to produce a second combustion chamber dual stage combustion product gas.
Owner:AUTOLIV ASP INC

Friction stir grain refinement of structural members

The present invention provides an improved structural assembly constructed of a plurality of structural members secured together. At least one of the plurality of structural members defines a first region characterized by comparatively high operational stress and a second region having a locally refined grain structure positioned such that the second region at least partially encompasses the first region to thereby enhance the strength, toughness and fatigue resistance of the at least one structural member in the first region. The present invention also provides a method for selectively improving the strength, toughness and fatigue resistance of a structural member in a region of high operational stress including the steps of casting the structural member in a pre-selected configuration. Regions of the structural member having comparatively high operational stress are identified. The structural member is secured to prevent movement. The region of the structural member having comparatively high operational stress is then mixed with a rotating friction stir welding probe to locally refine the grain structure of the structural member within the region of high operational stress to thereby improve the strength, toughness and fatigue resistance of the structural member in the region. The structural member can be secured to other structural members to form the frame of an aircraft. The improved structural assembly will have an increased operational life, as well as require less stock material with a corresponding decrease in the overall weight of the assembly.
Owner:THE BOEING CO

Seawater desalinator

The invention relates to a seawater desalinator, in particular to a seawater desalination device which overcomes the defects of high energy consumption and low efficiency of the prior art and is used for desalinating seawater. The seawater desalination device comprises a hollow shaft, an upper bearing cover, an upper end bearing, a lower end bearing, an upper end cover, a stator part, a rotor part, a lower end cover, a lower bearing cover, a water-containing pan and two sealing sleeve assemblies. When the seawater desalination device is in work, seawater flows in the device from the hollow shaft and enters a cavity chamber with the stator part and the rotor part, external power drives the rotor part to rotate, the seawater is magnified by an electromagnetic reaction between the stator part and the rotor part and heated by generated heat, the rotating speed of the rotor part is increased after magnification is finished, a sealing pressure block is opened by utilizing centrifugal force which is generated by the high-speed rotation, the seawater enters a cavity of an outer cylinder body through a film and a film sealing sleeve, and fresh water flows in the water-containing pan. The invention changes the acting force between the solute and the solvent of an aqueous solution by a magnetic field, improves the flux of the film, increases the seawater temperature and enhances the water permeation capability.
Owner:HARBIN INST OF TECH

Clean coal pressurized fluidized bed slag gasification process and system

The invention discloses a clean coal pressurized fluidized bed slag gasification process and system. By means of the gasification process and system, the problems that an existing pressurized fluidized bed industrial gasification process is complex, poor in coal applicability, low in gasification pressure, small in production capacity and low in gasification efficiency, the environment is polluted are solved. According to the technical scheme, the process includes the steps that raw material coal powder is pressurized and sent to a fluidized bed gasification furnace through a material inlet to react with a gasifying agent in a gasification mode, and crude synthesis gas and coal powder ash slag are obtained; the crude synthesis gad rises and is sent to a multi-pipe type cyclone separator through a top outlet of the fluidized bed gasification furnace to be dedusted, fluidizing agents are sprayed twice through a gasification spray nozzle to improve gasification efficiency, the coal powder ash slag is melt through a slag melting device, forms melt slag and then enters a slag quenching tank through a bottom outlet of the fluidized bed gasification furnace to be quenched and discharged through a slag locking hopper. The clean coal pressurized fluidized bed slag gasification process and system are simple in process, easy and convenient to operate, wide in coal applicability, high in gasification pressure, large in production capacity, high in gasification efficiency and environmentally friendly.
Owner:WUHUAN ENG +1
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