72results about How to "Increase swirl intensity" patented technology

The invention provides a sewage processing method, solving the problems of unsatisfactory effect of the sewage processing and the existing dead end of the sewage processing in a prior technology. The method comprises the following steps: adding medications into the sewage; flowing the mixed liquor into a cyclone reactor tangentially to perform cyclone separate; performing magnetic separation process on the mixed liquor after being cyclone separated through a magnetic roller. Meanwhile, the invention also provides a sewage processing device adopting the method; the device consists of a sewage inlet pipe, a clear water outlet pipe, a medication-adding system, a cyclone reactor, a magnetic roller and a scraper. The medication-adding system is connected with the sewage inlet pipe; an outlet end nozzle of the sewage inlet pipe is connected tangentially into the cyclone reactor, the cyclone reactor is a revolving body, the magnetic roller and the scraper are positioned in the cyclone reactor, the magnetic roller and the cyclone reactor are arranged on a same axial-line, and the scraper is used to scrape ferromagnetism mud cluster which is absorbed magnetically on the magnetic roller. In the invention, sewage purification has a good effect, the yielding water is clear, sewage processing method and sewage processing device of the invention are applicable to processing the sewage and the sewage containing grease and mud.

The invention provides a cyclone dust removal device which comprises a cyclone cylinder, wherein an air inlet is formed in a top side face of the cyclone cylinder; an exhaust pipe stretching into thecyclone cylinder is arranged at the top of the cyclone cylinder; an ash bucket is arranged at the lower part of the cyclone cylinder; an inverted cone is arranged at the bottom in the cyclone cylinder; a gap is reserved between the periphery of the inverted cone and a conical cylinder part of the cyclone cylinder. According to the cyclone dust removal device disclosed by the invention, the separation efficiency of dust particles can be improved, and secondary back-mixing discharge of the dust is avoided.

The invention discloses a liquefied gas combustion chamber with an outlet equipped with swirling vanes. The liquefied gas combustion chamber adopts a single-tube cylindrical combustion chamber structure and mainly comprises a liquefied gas spray nozzle, a combustion chamber case, a flame tube and the swirling vanes, wherein the swirling vanes are welded to strip-shaped grooves of the flame tube, form certain angles with the axial direction and are uniformly distributed circumferentially; the flame tube and the case are connected by a bolt; liquefied gas enters the head of the combustion chamber from an oblique hole of the spray nozzle, and the combustion of the liquefied gas is completed by using an electrospark lighter; a combustion organization generates strong-swirl stable flame by adopting internal-external two-stage swirlers, and a cooling manner is an impact wall-divergence wall coupled vane gas film hole manner; the swirling direction of an external swirler is the same as that of the swirling vanes of the outlet of the combustion chamber, due to the coupling of swirling, the strength of swirling in the flame tube is strengthened, and the length of flame is shortened; high-temperature combustion gas generated from combustion generates relatively-strong swirling flow when the high-temperature combustion gas passes through the swirling vanes, the high-temperature combustion gas is exhausted from the outlet of the combustion chamber and forms expanding gas flow, and thus, the radial distribution of outlet combustion gas in space is enlarged.

The invention provides a cavity trapped vortex and rectifying support plate combined type integrated afterburner. The ignition stability can be improved effectively, and the swirling intensity of a backflow area and the fuel atomization effect are improved, so that the combustion efficiency and stability are improved. A rectifying support plate flame stabilizer is combined with cavity trapped vortex; on one hand, air flow of inner and outer ducts enters a cavity from different positions, and a trapped vortex area is formed; duty-level flame is generated, so that mixed gas of a main flow area is ignited; on the other hand, a stable main backflow area with a certain gas backflow amount and in an appropriate size is formed downstream; and ignited high-temperature air and air in the outer ductare promoted to mix, and play a role in rectification and stabilization of combustion. The integrated afterburner has the advantages that the structural design of a cavity duty stabilizer is added atthe rear edge of the rectifying support plate flame stabilizer on the original basis of the integrated afterburner, and the ignition ability under the rich oil and high altitude conditions can be improved effectively; and the high combustion stability and efficiency are ensured.

An intensive-classification low-NOx pulverized coal burner comprises a primary air passage, a direct-flow inner secondary air passage and a cyclone inner secondary air passage; pulverized coal is separated by a coal flow equalizer and a pulverized coal separator disposed in the primary air passage into thick-inside thin-outside structure at a spout, blown into a hearth; the inner secondary air passage is provided with a direct-flow air inlet and a cyclone air inlet; secondary air is mixed in the inner secondary air passage and spayed into the hearth; volume of the direct-flow air is controlled through a pull rod, so that cyclone strength of the inner secondary air can be controlled. Each of primary and secondary air outlets is provided with a certainly angular spout expanded-cone structure, real-time mixing of the secondary air and the pulverized coal is effectively controlled, a spout water-cooling wall is in the oxidization atmosphere in a long period of time meanwhile, and slag buildup and high temperature corrosion can be effectively prevented for the water-cooling wall in a burner area. The intensive-classification low-NOx pulverized coal burner has the advantages that combustion stability is high, adjusting performance is good, the burner is well adaptable to various coals, and emission of nitric oxide is low.

A pilot-type differential valve with metering function for the water meter system with IC card pre-charge function features that the meter, blade wheel, permanent-magnetic ring and guide cover of traditional water meter and the partition, piston, valve plug and valve seat of pilot-type differential valve are assembled in a single casing, and a specia blade wheel structure is used, which features that the blade wheel is separated from its axle for moving up and down under the action of spring. Its advantages include light weight low cost small size.

The invention relates to a gas turbine low-pollution combustion chamber single-vortex head structure. Firstly, central vortex air and central natural gas are mixed, and outer wall non-vortex air and outer wall natural gas are mixed. After that, the vortex air, the non-vortex air, the central natural gas and the outer wall natural gas are further mixed in a natural gas-air mixing cavity, the mixinguniformity of the natural gas and air can be improved, generation of hot spots can be avoided, and generation of nitric oxide is effectively lowered. By means of the gas supply mode of combination ofcentral vortex and outer wall non-vortex, the vortex intensity of head outlet airflow can be lowered, and the risk of occurrence of oscillation combustion is also lowered. By means of the combinationof the central natural gas and outer wall natural gas, the NOx-CO proportion can be improved, and flame stability is facilitated. A head outlet convergence section can improve the speed of natural gas-air mixed airflow, and tempering is effectively prevented. A tangential gas inlet small hole in the outer wall of a whirlcone can lower the risk of spontaneous combustion occurring inside the head structure.

The invention aims to provide a double-flap swirl-type dual-fuel nozzle used for a chemical regenerative cycle. The double-flap swirl-type dual-fuel nozzle comprises an auxiliary oil-path channel wall, a main oil-path channel wall, a gas-path outer wall and an oil-path spout. An auxiliary oil-path channel is formed inside the auxiliary oil-path channel wall, and an auxiliary oil-path swirler is arranged at the end of the auxiliary oil-path channel wall and communicated with the oil-path spout. The main oil-path channel wall is arranged outside the auxiliary oil-path channel wall, and a main oil-path channel is formed between the main oil-path channel wall and the auxiliary oil-path channel wall and communicated with the oil-path spout. The gas-path outer wall is arranged outside the main oil-path channel wall, and a gas-path channel is formed between the gas-path outer wall and the main oil-path channel wall. Flap type swirl cavities are formed in the end, located on the oil-path spout, of the gas-path outer wall, and gas injection holes are formed in the end faces of the flap type swirl cavities and communicated with the gas-path channel. According to the double-flap swirl-type dual-fuel nozzle, the flow speed is decreased, the swirl speed is pre-increased, and mixing of gas fuel and air is enhanced. When liquid fuel is combusted independently, water vapor reinjection can also be conducted through a gas path, and NOx emission is reduced.

The invention provides a suspension smelting method. According to the method, the heating speed and the reaction speed of materials are increased by a central backflow area and/or an external backflow area as well as grading reaction; by the aid of higher cyclone intensity, mixing uniformity of the materials and oxygen-enriched air is improved, and the suspension time of the materials in a reaction tower is increased; metallurgy reaction proceeding and sufficient reaction are promoted remarkably, the productivity of a flash furnace is improved, and suspension smelting of concentrate containing high impurities is realized better. The invention further provides a suspension smelting nozzle for implementing the suspension smelting method.

The invention discloses a swirling piece, a swirling burner and a manufacturing method of the swirling burner and relates to the field of swirling combustion equipment adopting the swirling piece. The swirling piece comprises a swirling piece body. An against-wind section is arranged at one end of the swirling piece body, and a wind outlet section is arranged at the other end of the swirling piece body. Fluid flows towards the wind outlet section from the against-wind section. The thickness of the against-wind section is gradually increased in the flowing direction of the fluid till being the same as that of the swirling piece body. The swirling burner comprises an inner pipeline, an outer pipeline, one swirling piece arranged on the inner wall of the inner pipeline, one swirling piece arranged on the outer wall of the inner pipeline and/or one swirling piece arranged on the inner wall of the outer pipeline, wherein, the inner pipeline is sleeved with the outer pipeline. According to the swirling piece, the swirling burner and the manufacturing method of the swirling burner, pressure loss after the high speed fluid passes through the swirling piece can be reduced by the swirling piece and the swirling burner at low cost, and the mounting procedure of the swirling piece can be greatly simplified through the manufacturing method of the swirling burner.

The invention discloses a W flame boiler provided with turbulent burners and direct flow burners and relates to a pulverized coal boiler, and belongs to the technical field of boiler combustion. The Wflame boiler provided with the turbulent burners and the direct flow burners aims to solve the problem the flow field in the W flame boiler deflects. The W flame boiler provided with the turbulent burners and the direct flow burners comprises an upper hearth, a lower hearth, a front furnace arch, a rear furnace arch and a plurality of graded air spray ports, and further comprises the plurality ofturbulent burners and the plurality of direct flow burners; each turbulent burner comprises a primary air channel I, a secondary air channel I and blades; the secondary air channels are arranged outside the primary channels in a sleeving manner; the blades are arranged in the secondary air channels I; each direct flow burner comprises a primary air channel II and a secondary air channel II; the upper hearth is arranged above the lower hearth; the front furnace arch is provided with one row of the turbulent burners in the hearth width direction; the rear furnace arch is provided with one row of the direct flow burners in the hearth width direction; and a plurality of the graded air spray ports are formed in a front wall in the hearth width direction, and a plurality of the graded air sprayports are formed in a rear wall in the hearth width direction.

The invention provides a sand discharge funnel. The sand discharge funnel comprises a water inlet culvert, an edge wall, a funnel chamber, a flow adjusting suspension plate, an overflow weir and a side groove; the water inlet culvert is connected to the upper portion of the funnel chamber, and is tangential to the outer periphery of the funnel chamber; and a sand discharge bottom hole is formed inthe bottom of the funnel chamber, and is connected to a sand discharge gallery. The edge wall is connected to the upper portion of the funnel chamber to form a first arc section envelope structure. The overflow weir is connected to the upper portion of the funnel chamber to form a second arc section envelope structure. The flow adjusting suspension plate is provided with a center-near end and a center-far end; the center-far end is connected to the upper end of the overflow weir; and the center-near end is near the center of the funnel chamber and higher than the center-far end. The side groove is connected to one side of the overflow weir to form a third arc section envelope structure with the edge wall; and a drainage ditch port is formed in the side groove. Through structural improvement, the problems of bad sediment accumulation at the bottom of the funnel chamber and on the suspension plate and high sand discharge water consumption rate are solved, and the sand discharge efficiency of the sand discharge funnel is improved.

The glass kiln with emulsified coke slurry burner includes one kiln body and one emulsified coke slurry burner. The kiln body includes one hearth, one flame inlet and one fume outlet. The emulsified coke slurry burner includes one casing forming one inside cylindrical burning space, at least one emulsified coke slurry burning unit, at least one oil/gas burner, one outlet communicated via hot blast pipe to the flame inlet of the hearth. The glass kiln includes also two or more switchable heat accumulating chambers connected via pipeline with the fume outlet of the kiln body. The present invention has double heat accumulation with lattice brick and ceramic ball reaching a heat accumulating temperature as high as 1200 deg.c to make up the low heat value emulsified coke slurry.

The invention discloses to a multichannel rotational flow coal burner and relates to a rotational flow coal burner, and the multichannel rotational flow coal burner is used for solving the problems that the coal dust flame of the existing rotational flow coal burner has bad stability, and the burning is insufficiency and the perfect diffusion airflow exists. The burner provided by the invention is characterized in that one end of a primary air pipeline is arranged in a secondary air first pipeline, and the secondary air first pipeline is arranged in a secondary air second pipeline; the secondary air second pipeline is arranged in a secondary air third pipeline, and the secondary air third pipeline is arranged in a secondary air regulating pipeline; a first swirler is arranged in the secondary air first pipeline, and a second swirler is arranged in the secondary air second pipeline; and the ventilation door of the secondary air third pipeline is arranged in the secondary air third pipeline, and the ventilation door of the secondary air regulating pipeline is arranged in the secondary air regulating pipeline. The rotational flow coal burner provided by the invention is used for boiler combustion.

The invention relates to an adjustable swirl blade assembly and a flat flame burner comprising the same, and belongs to the technical field of combustion equipment. The adjustable swirl blade assembly comprises an adjustable swirl blade assembly body and a blade transmission device, and the body comprises a central rectification body, an outer cylinder, an inner cylinder and a plurality of rotatable blades which are coaxially arranged; the blade transmission device comprises a plurality of blade rotating shafts which are fixedly connected with the blades and are used for controlling the blades to rotate, transmission connecting rods which are fixedly connected with one ends of the blade rotating shafts in a one-to-one correspondence manner, a total connecting ring which is connected with the transmission connecting rods and surrounds the adjustable swirl blade assembly body, and an operating rod which is connected with the total connecting ring and is used for controlling the total connecting ring to move; and each transmission connecting rod is formed by rotationally connecting three rigid connecting rods, and two rotating pairs with non-coaxial lines and non-parallel rotating shafts are formed at the joint. The technical problem that in a traditional device, control over blades is not accurate is solved, a combustor can operate under the small-load working condition, the large air-fuel ratio working condition and the condition that the fuel heat value fluctuates violently, and stable flat flames are formed.

The invention provides a plasma nozzle, the plasma nozzle comprises an outer cylinder, a middle cylinder, an axial suspending plate, at least one power supply and at least one plasma actuator, wherein the axial suspending plate is arranged between the outer cylinder and the middle cylinder; the power supply is used for providing excitation voltage for the plasma actuator; and the plasma actuator is arranged on the axial suspending plate and is used for generating plasma under the function of the excitation voltage. According to the invention, the flowing induced by the plasma can form free jet on the edge of the axial suspending plate, so that the dissipation for flowing momentum induced by the plasma from a wall boundary layer is eliminated, the swirling intensity can be effectively enhanced, and the burning is stable.

The invention is the outer cyclone inner direct flow main combustor device and belongs to the combustor device of boiler. The purpose of the invention is to produce the backflow area and the stable combustion. One device of the invention is to evenly arrange the delivery blades between the primary air diverting tube and the delivery tube, and the inside diameter of the delivery tube is as 0.5-0.7 times as the diameter of the primary air diverting tube. The other device is to evenly arrange the delivery blades in the inner chamber of the primary air diverting tube, and the axial height of the delivery blades is as 0.1-0.5 time as the semi-diameter of the primary air diverting tube. The invention through changing the opposite angles, the number, the length and the height of the delivery blades and the lengths and the section of the delivery tube to change the intensity and the size of the cyclone amount to adapt the characteristics of different fuels and ensure the stability and economy of the boiler combustion. The invention has simple structure and convenient equipment.

The embodiment of the invention relates to an under-well double-vortex type rotational flow oil and water separator. The separator is an under-well rotational flow oil and water separation plant usinga high-speed rotational flow principle, and compared with a traditional hydrocyclone, the separator comprehensively uses double same-direction rotational flows for pre-separating oil and water and double opposite-direction rotational flows for conducting under-well refining oil-contained waste water treatment. In the pre-separation process of the oil and the water, two phases of the oil and the water move in the same axial direction in a rotational flow field, so that the two phases of the oil and the water are barely mixed compared with those conducting rotational flow motion in the oppositeaxial directions, a separation effect is better, and accuracy is higher; and in the oil-contained waste water treatment process, a long and thin cone is used for increasing the rotational flow intensity, so that the oil content of the separated water phase is lower. Compared with a traditional gravity sedimentation plant, the separator is better in treatment effect and smaller in occupied space and is a physical separation plant with application prospects.

The invention provides a low-pressure rotational flow bubble type nozzle. The low-pressure rotational flow bubble type nozzle comprises a flow distribution chamber, a tangential water inlet pipeline,an axial water inlet pipeline, a mixed flow pipe and a gas-liquid mixing cavity; an outlet of the flow distribution chamber is communicated with each the tangential water inlet pipeline and the axialwater inlet pipeline, the outlet of the axial water inlet pipeline is communicated with the mixed flow pipe, and a rotational flow device is arranged in the axial water inlet pipeline and used for generating rotational flow to enter the mixed flow pipe; the outlet of the tangential water inlet pipeline is in tangent connection with the mixed flow pipe and is used for generating tangential flow; the mixed flow pipe is used for converging the rotational flow and the tangential flow; the gas-liquid mixing cavity is communicated with the mixed flow pipe, and the outlet of the gas-liquid mixing cavity is connected with the nozzle. The low-pressure rotational flow bubble type nozzle provided by the invention can generate rotary bubble type water drops, not only increases the cleaning area and enhances the cleaning effect, but also has the massage and striking effect, the blood circulation of the human body is promoted, and the human body has more comfortable skin feeling.

The invention discloses a heat-conducting oil stove used the emulsifying burnt plasma vortex burning device. It includes the oil stove body and the emulsifying burnt plasma vortex burner which includes the shell composed by the front wall, the back wall and the side wall. The burning room is formed in the shell. At least one emulsifying burnt plasma vortex burner and at least one oil burner or at least one gas burner is set in the front wall; an outlet is set in the back wall which is connected with the flame inlet of furnace chamber by the warm-air pipe. The two or above groups of tangential wind inlets are set on the shell side wall alternately; the outlet of the liquid slag is on the side wall of the burning room bottom which is near to the back wall. The invention uses the emulsifying burnt plasma as the fuel, so it can save the cost.

The present invention discloses a steam-injecting boiler adopting emulsified coke slurry combustion equipment. It includes boiler self-body and emulsified coke slurry combustion equipment. Said boiler self-body includes furnace cavity, at least one steam pipe set in the furnace cavity interior and smoke outlet cut on one end wall far-separated from the emulsified coke slurry combustion equipment. Said emulsified coke slurry combustion equipment includes a shell body formed from front end wall, rear end wall and side wall, a cylindrical combustion space is formed in the shell body, on the front end wall at least one emulsified coke slurry combustor, at least one oil combustor and/or at least one gas combustor are set, its rear end wall is equipped with an outlet, said outlet is communicated with furnace cavity.