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126results about How to "Large flow cross-sectional area" patented technology

All natural circulation-type modular small reactor

The invention discloses an all natural circulation-type modular small reactor. The all natural circulation-type modular small reactor comprises a reactor main body, a safe shell, a water tank and a passive safety system. The reactor main body comprises a pressure vessel. A reactor core, a direct current steam generator and a voltage stabilizer are orderly arranged in the pressure vessel from bottom to top. One end of a control rod driving mechanism matched with the reactor core is arranged at a top cover of the pressure vessel. The pressure vessel is arranged in the safe shell. The safe shellis immersed in the water tank. The passive safety system comprises a passive residual heat removal system and a passive safe shell heat transmission system. The reactor is free of forced circulation of a path of a cooling agent driven by a main pump, and utilizes density contrast of cooling agents between the direct current steam generator and the reactor core and cold and hot core potential difference to drive the cooling agents to all naturally circulate in the pressure vessel so that the reactor safety is improved. The passive safety system realizes a lasting submerged state of the reactorcore and carries out the residual heat of the reactor core to prevent core damage.
Owner:NUCLEAR POWER INSTITUTE OF CHINA

Large box type high-temperature material heat exchanger

The invention provides a large box type high-temperature material heat exchanger, and belongs to the field of high-temperature solid material cooling equipment. The large box type high-temperature material heat exchanger is characterized by sequentially comprising a water cooling box cover (2), a heat exchanging box (6) and necking-down type hoppers from top to bottom, wherein a water cooling jacket is arranged on a wall of the water cooling box cover (2); end water cavities and / or side water cavities are formed in the wall of the heat exchanging box (6) and the walls of the necking-down hoppers; a plurality of heat exchanging pipelines are respectively arranged in the water cooling box cover (2), the heat exchanging box (6) and cavities of the necking-down type hoppers; a feeding opening (1) is formed in the upper portion of the water cooling box cover (2); a water cooling spiral distributor (3) which can convey and cool down materials is arranged in the water cooling box cover (2); the necking-down type hoppers are arranged side by side; and an impeller discharging valve (8) is arranged at an outlet of the bottom of each necking-down type hopper. The large box type high-temperature material heat exchanger is large in material cooling amount, low in energy consumption and long in service life; and abrasion of heat exchanging components is small.
Owner:SHANDONG UNIV OF TECH

Biomass gasification power-generation process

The invention discloses a biomass gasification power-generation process. The biomass gasification power-generation process comprises the following steps of step (I), pressurizing biomass granules until the gauge pressure is 0.1-4.0Mpa, then discharging materials to a charging tank, then conveying the discharged materials to a fluidized-bed gasifier, and performing a gasification reaction with a gasification agent so as to obtain fuel gas for standby application; step II, performing cyclone dust removal on the fuel gas prepared in step (I) through a cyclone separator, performing separation to obtain large particles which are not burn-out, and returning the large particles to the fluidized-bed gasifier for gasifying once again; and step (III), cooling the flue gas which is subjected to dust removal by the cyclone separator to 300-700 DEG C through a heat exchanger, and enabling the cooled flue gas to be led into a coal boiler to be subjected to mixed combustion with the coal for power generation. According to the biomass gasification power-generation process disclosed by the invention, the biomass granules are sent to a large-scale coal boiler through the fuel gas generated by gasification to be subjected to combined combustion with the coal for power generation, so that the coal consumption required for power generation is reduced, the amount of CO2 generated during combustion is reduced, greenhouse effects caused by CO2 can be alleviated, and emission of NOX by power plants is reduced.
Owner:武汉高斯生态能源技术有限公司

Coalescence degreaser for oilfield sewage treatment

ActiveCN111348769AThe number of deployments increasedSolve the problem of stable loweringWaste water treatment from quariesFatty/oily/floating substances removal devicesFiberYarn
The invention provides a coalescence degreaser for oilfield sewage treatment. The coalescence degreaser comprises a tank body, a flow stabilizing device, a rectifying device, a primary filtering device and an oil gathering device; the tank body sequentially comprises a lining layer formed by jet yarns in a jet molding mode, a structural layer formed by resin and fiber material composite materialsin an enveloping and winding mode and an outer surface layer formed by gel coat resin in a spraying mode from inside to outside in the thickness direction of the tank wall. The oil gathering device comprises a coalescence separation corrugated plate and a supporting piece. The thickness of corrugated plates in the prior art is reduced to increase the cross sectional area of a water flow channel between the adjacent corrugated plates, so that the sewage treatment capacity is greatly improved; and on the premise that the sewage treatment efficiency is not reduced, namely, the cross section of the water flow channel is kept unchanged, the arrangement number of the corrugated plates is greatly increased, so that the contact area of the corrugated plates and sewage is increased, and the oil gathering efficiency and effect are improved.
Owner:SHENGLI OIL FIELD XINDA PIPE IND TECH DEV CO LTD

Upper straight-down rotating dry-type circulating fluidized bed desulfurization reactor

InactiveCN101496991AIncreased cross-sectional area of ​​flue gas flowExtended stayDispersed particle separationChemical/physical processesEngineeringFluidized bed
The invention discloses a desulphurization reactor of an upper direct-lower rotary dry-type circulating fluidized bed and relates to a desulphurization reactor of the circulating fluidized bed. The reactor solves the problems that the prior desulphurization reactor has low working efficiency and particles are easy to cling to the wall surface and the prior desulphurization reactor has large height. An inner cylinder is arranged in an outer cylinder; the lower end of the inner cylinder is positioned on the lower part of the outer cylinder; a swirler is arranged at the upper end of the inner cylinder; one to four tangential cyclone smoke exhaust pipes are positioned on the lower part of the outer cylinder and are evenly distributed on the outer sidewall of the inner cylinder along the tangential direction; each tangential cyclone smoke exhaust pipe is communicated with a cavity between the outer cylinder and the inner cylinder; the upper end of the shell is communicated with an inner cavity of the outer cylinder; the lower end of the shell is communicated with the inner cylinder; one side of each cyclone plate is connected with a central shaft; and the other side of each cyclone plate is connected with the inner wall of the shell. The desulphurization reactor has a compact structure, strong applicability of load change and low cost and is convenient for general layout and operating maintenance of the system; and the desulphurization efficiency is improved over 10 percent.
Owner:HARBIN INST OF TECH

U-shaped plate type dielectric-barrier-discharge-based low-temperature plasma reactor and reactive system

ActiveCN105050304AFlow adjustableChange the size of the flow cross-sectional areaPlasma techniqueGas passingEngineering
The invention relates to a U-shaped plate type dielectric-barrier-discharge-based low-temperature plasma reactor and reactive system. The reactor comprises a core electrode, a U-shaped plate electrode housing, an insulating medium and a driving power. The core electrode is installed inside the U-shaped plate electrode housing; and gas outlet channel parallel to the core electrode is arranged at the arc position of the U-shaped plate electrode housing. The insulating medium is installed between the core electrode and the U-shaped plate electrode housing. The driving power is respectively connected with the core electrode and the U-shaped plate electrode housing. Gas enters the reactor through a U-shaped opening of the U-shaped plate electrode housing; and the processed gas leaves the reactor through the gas outlet channel. According to the reactor, large-flow gas can be processed; the gas disturbance can be enhanced and the plasma catalysis can be strengthened; the mixed uniform degree of several kinds of gas can be improved; the dielectric barrier discharge (DBD) breakdown voltage and discharging power are low and the waste gas treatment cost can be lowered; and the reactor can work separately or work in a matrix arrangement mode.
Owner:SHANDONG ELECTRIC POWER ENG CONSULTING INST CORP

Villous fin fiber composite groove type special-shaped heat pipe and manufacturing method thereof

The invention discloses a villous fin fiber composite groove type special-shaped heat pipe. The villous fin fiber composite groove type special-shaped heat pipe comprises a heat pipe body with a special-shaped section. Grooves are formed in the inner wall of the heat pipe body. A villous fin fiber layer is laid on the inner wall of the heat pipe body. Villous fin fibers are metal fibers which are provided with irregular protrusions and/or pits on surfaces and are of a villous fin structure. The invention further discloses a manufacturing method of the villous fin fiber composite groove type special-shaped heat pipe. According to the villous fin fiber composite groove type special-shaped heat pipe, the capillarity attraction of a heat pipe wick is effectively improved, split-flow of liquid and steam inside the heat pipe is realized, the heat transfer performance of the heat pipe is effectively enhanced, the defect that groove type heat pips are low in threshold power is overcome, liquid permeability is improved, the resistance of working medium backflow is reduced, and the defect that traditional groove type heat pipes cannot be bent or flattened is overcome; and the heat pipe is a special-shaped pipe, so that the air flow section area is increased, air resistance is effectively reduced, the cooling air flow quantity is increased, and heat exchange performance is improved.
Owner:CRRC +1

Rotor assembly, compressor and air conditioner

The invention relates to the technical field of gas compression devices, in particular to a rotor assembly, a compressor and an air conditioner. A plurality of main circulation channels are evenly formed in a first magnetic baffle, a rotor iron core and a second magnetic baffle of the rotor assembly around the central axis, auxiliary circulation channels which are through in the axial direction are formed in the first magnetic baffle, the rotor iron core and the second magnetic baffle, a main balance block is located on one side of the central axis, and auxiliary circulation channels are located on the other side of the central axis. The auxiliary circulation channels improve a balance system, the height of the main balance block in the axial direction can be reduced, then the windward area of the main balance block is reduced, the clapping effect on exhaust gas flow is weakened, tiny liquid drops are reduced, and then the amount of oil entering an upper cavity of a motor along with flowing of a refrigerant is reduced. The auxiliary circulation channels increase the flow flowing through the circulation channels, improves the internal circulation of the compressor, increases the stator trimming return flow, and realizes secondary oil separation. The effects of two oil separation are integrated, and the oil spitting rate of the compressor is effectively reduced.
Owner:GREE ELECTRIC APPLIANCES INC

Efficient heat exchange structure of compressed air refrigeration dryer

The invention provides an efficient heat exchange structure of a compressed air refrigeration dryer. The problems that according to existing equipment, ice blockage is prone to occurring, the structure is incompact, and the drying effect is poor can be solved. The efficient heat exchange structure comprises a vertically-arranged first pipe and further comprises a second pipe arranged in an inner cavity of the first pipe; a first cavity is formed between the inner wall of the first pipe and the outer wall of the second pipe; an inner cavity of the second pipe forms a second cavity, and the upper portion of the second pipe is provided with an air inlet and communicates with the second cavity; the second pipe is provided with a plurality of first heat exchange pipes in a vertical penetratingmode, and bottom ends of the first heat exchange pipes communicate with the first cavity; a connection pipe is arranged in the second pipe, the top end of the connection pipe communicates with the upper portion of the first cavity, and the bottom end of the connection pipe communicates with the lower portion of the second cavity; and the bottom of the first pipe is provided with a water collectingtank and a drain pipe. The efficient heat exchange structure is compact in structure, resistant to corrosion, free of secondary pollution, small in pressure loss, capable of reducing ice blockage andleakage phenomena, simple in technology, low in cost and good in water-air separation effect.
Owner:FOSHAN TIANDI YUANYI PURIFICATION EQUIP

Ultra-low-nitrogen combustion equipment with post-premixing cold flame combustion coupling matrix tube mode wall structure

The invention relates to ultra-low-nitrogen combustion equipment with a post-premixing cold flame combustion coupling matrix tube mode wall structure. The ultra-low-nitrogen combustion equipment comprises a fuel gas regulation and control device, an air volume regulation and control device, an air-gas mixing device, a cold flame combustion device, a matrix tube and mode wall device and a comprehensive controller. The fuel gas regulation and control device provides fuel gas for the air-gas mixing device; the air volume regulation and control device provides combustion-supporting air for the air-gas mixing device; the air-gas mixing device conducts jet flow mixing on combustible gas provided by the fuel gas regulation and control device and the combustion-supporting air provided by the air volume regulation and control device, and the combustible gas and the combustion-supporting air are evenly mixed through the air-gas mixing device and then injected into the cold flame combustion device; the mixed gas sequentially passes through a double-layer rectifying plate, a hexagonal heat pipe type cooling fire-retardant tube nest and a flame cooling tube nest in the cold flame combustion device and then enters a combustion chamber for combustion; and after combustion, high-temperature flue gas is subjected to radiation and convective heat exchange in the combustion chamber, then exchanges heat with a medium in the matrix tube and mode wall device and then is discharged into a flue.
Owner:BEIJING BOOSTER BOILER

Organic heat carrier waste-heat furnace and waste-heat furnace system

The invention discloses an organic heat carrier waste-heat furnace which comprises a waste-heat furnace body and a settling chamber, wherein one side wall of the settling chamber is provided with a smoke inlet, and the other side wall of the settling chamber is connected with one side of the waste-heat furnace body through a flue; the other side wall of the waste-heat furnace body is provided with a smoke outlet, the settling chamber is internally provided with a settling chamber diaphragm-type wall pipe screen, the top of the settling chamber diaphragm-type wall pipe screen is connected with the top of the settling chamber, and the bottom of the settling chamber diaphragm-type wall pipe screen is provided with a smoke channel; the waste-heat furnace body is internally provided with a plurality of mutually parallel convection sections, each adjacent convection sections are separated by smoke folding devices, each adjacent smoke folding devices are arranged in a stagger manner, and smoke entering the adjacent convection sections turns; and the convection sections comprise a plurality of pipe screens which are mutually parallel arranged, the spacing between each adjacent pipe screens is more than 100 mm, the design can be used for ensuring the smoke entering the adjacent convection sections to turn, increasing the disturbance of the smoke, realizing the effective segregation of the smoke, reducing the smoke flow rate and reducing the abrasion of a heating surface.
Owner:WUXI XINENG BOILER

Compressed gas refrigerated dryer heat exchanging water removal structure

The invention provides a compressed gas refrigerated dryer heat exchanging water removal structure which can improve the problems that the existing equipment is not impact in structure, and poor in gas and water separating effect and can cause ice blockage easily, and the inlet and outlet differential pressure of compressed gas is large. The compressed gas refrigerated dryer heat exchanging waterremoval structure comprises a first pipe vertically arranged, and a second pipe arranged in the first pipe, wherein the bottom of the second pipe is not in contact with the bottom of the first pipe; agas-liquid separation cavity is formed between the first pipe and the second pipe; a liquid collecting cavity is formed in the bottom of the gas-liquid separation cavity; a refrigerating cavity is formed in the second pipe and is provided with a refrigerating source outlet and a refrigerating source inlet; the refrigerating cavity communicates with a gas inlet; the compressed gas refrigerated dryer heat exchanging water removal structure further comprises one or more third pipes; one end of the third pipe communicates with the external world and serves as a gas outlet; the other end of the third pipe communicates with the upper part of the liquid collecting cavity; the gas enters from the gas inlet, is cooled through the refrigerating cavity and is subjected to gas-water separation through the gas-liquid separation cavity, then, condensate separates out and flows to the liquid collecting cavity, and the gas is discharged out of the gas outlet through the third pipe.
Owner:FOSHAN TIANDI YUANYI PURIFICATION EQUIP

Undisturbed switching control method of pneumatic regulation valve

The invention discloses an undisturbed switching control method of a pneumatic regulation valve. The undisturbed switching control method of the pneumatic regulation valve relates to a device body anda first cavity formed in the device body. A first rotary shaft which extends upwards and downwards is rotatably arranged in the first cavity. The tail end of the top of the first rotary shaft is in power connection with a motor fixedly arranged in the top end wall of the first cavity. According to the undisturbed switching control method of the pneumatic regulation valve, the structure of a device is simple, the performance is reliable, and mounting, maintenance and repair are convenient; the device can automatically detect the rate of flow passing through the device and compares the flow rate with an initial setting, automatic dynamic regulation is conducted according to the flow rate, and thus, it is ensured that the rate of flow passing through the valve is constant; meanwhile, the device can be switched into a manual mode according to requirements, the flow data and the operating state of the device are not changed in the switching process, and thus, undisturbed switching betweenthe automatic mode and the manual mode is achieved; and in addition, the device can generate compressed gas through a micro gas pump, and an external gas source is not needed, so that the mounting procedure is greatly simplified, and the maintenance cost of the device is reduced.
Owner:俞李娜

Large-area and high-thermal-conductivity light and thin microgroove flat heat tube

The invention discloses a large-area and high-thermal-conductivity light and thin microgroove flat heat tube, and belongs to the field of microgroove flat thermal control engineering. The large-area and high-thermal-conductivity light and thin microgroove flat heat tube comprises a microgroove shell, a microgroove cover plate and a liquid filling pipe, wherein the microgroove cover plate is fixedly mounted at the upper part of the microgroove shell; a reinforcing rib is arranged at the lower part of the microgroove cover plate; and the liquid filling pipe is fixedly mounted at the right side of the upper end of the microgroove shell. The invention provides the large-area and high-thermal-conductivity light and thin microgroove flat heat tube; firstly, a capillary structure, the cover plate and the shell are connected to form a complete sealing structure through modes of electronic beam welding, TIG welding and dissimilar metal brazing, so that the high heating flux can be realized, and the heat transfer on the larger heat transfer contact area is efficient and reliable; and the large-area and high-thermal-conductivity light and thin microgroove flat heat tube is relatively lighter in whole weight and higher in structural strength, can serve as a structural part and a bearing part, and is convenient for use. The large-area and high-thermal-conductivity light and thin microgroove flat heat tube reduces the system complexity, and improves the system reliability.
Owner:BEIJING SATELLITE MFG FACTORY

Blast furnace gas dry method bag type dust removing mechanical type pressure dust unloading process and device thereof

Disclosed is a blast furnace gas dry method bag type dust removing mechanical type pressure dust unloading process and device. A first gas pressure relief valve is arranged on a dust and gas chamber located on the lower portion of each cloth bag dust removing box body. Each first gas pressure relief valve of the corresponding cloth bag dust removing box body is connected to a concentration dust bin through a first gas pressure relief pipe, so that dust and gas with pressure in the concentration dust bin enter the dust and gas chambers located on the lower portions of the cloth bag dust removing box bodies through the first gas pressure relief valves. A second gas pressure relief valve is arranged on a gas purifying chamber located on the upper portion of each cloth bag dust removing box body. Each second gas pressure relief valve of the corresponding cloth bag dust removing box body is connected to a low pressure purified gas main pipe through a second gas pressure relief pipe, so that gas in gas purifying chambers located on the upper portions of the cloth bag dust removing box bodies enters the low pressure purified gas main pipe through the second gas pressure relief valves. Cloth bag dust removing box body dust unloading is conducted by utilizing gas pressure energy of a dust removing system. The blast furnace gas dry method bag type dust removing mechanical type pressure dust unloading process and device have the advantages that the mechanical dust unloading and conveying process is adopted and meanwhile pneumatic dust unloading and conveying are utilized, and the pneumatic dust unloading and conveying process is adopted and meanwhile mechanical power dust unloading and conveying are utilized.
Owner:LIUZHOU IRON & STEEL
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