6109results about "Flow mixers" patented technology

The invention relates to the technical field of homogenizing equipment, and discloses an adjustable gap type high-pressure microjet collision homogenizing valve structure and a homogenizing method.The homogenizing valve structure comprises a valve body provided with a homogenizing channel; the homogenizing valve seat is mounted in the homogenizing channel; the homogenizing valve seat is provided with a plurality of flow guide channels penetrating through the homogenizing valve seat, and the plurality of flow guide channels are arranged around the circumference at intervals; the homogenizing valve element is mounted in the homogenizing channel in a sliding manner; a jet flow cavity is formed between the homogenizing valve core and the homogenizing valve seat; a discharging hole is formed in the center of the homogenizing valve element, and an impact cavity is formed between the end of the discharging hole and the homogenizing valve seat and located in the center of the jet flow cavity. The adjusting device is used for driving the homogenizing valve core to slide and adjusting the distance between the homogenizing valve core and the homogenizing valve seat; wherein the discharging hole is aligned with the center of the homogenizing valve seat, and materials enter the jet flow cavity through the flow guide channel and then enter the discharging hole after being collided by the collision cavity. According to the homogenizing valve structure, the gap and the homogenizing pressure can be adjusted, and the purity of materials is not affected.

The utility model discloses a venturi multistage gas-liquid mixer with parallel jet nozzles, which comprises a liquid inlet pipe, an air suction chamber, a venturi pipe contraction pipe section, a venturi pipe throat pipe section and a venturi pipe diffusion pipe section which are connected in sequence, and a plurality of air inlet pipes are uniformly arranged on the same circumference of the outer side wall of the air suction chamber; seven liquid inlet jet spray pipes are arranged in the air suction chamber, and inlets of the seven liquid inlet jet spray pipes are jointly connected with a liquid inlet pipe. According to the utility model, the problem that gas and liquid cannot be fully mixed into a uniform phase due to low quality of generated bubble groups in the prior art is solved.

The present embodiments relate to systems and methods relating to a capsule containing a liquid concentrate and a device capable of creating a gas-infused liquid, such as a nitro-infused cold beverage or iced coffee. The device can include a cold-water tank and a cooling system to chill cold water. The device can also include a gas reservoir including a gas. The device can also include a fluidic capsule connector that includes capsule connector configured to connect to a capsule and establish a pressurized chamber in a cavity of the capsule that is removably connected to the capsule connector, a liquid entrance valve that can configured to provide a stream of cold water and gas to the pressurized chamber. The fluidic capsule connector can also include a dispense port configured to direct a flow of the gas-infused liquid from the pressurized chamber to a dispensing tap.

The invention provides a static mixer with a bionic starfish type inlet structure and a mixing method thereof. The static mixer comprises a shell, a cavity is formed in the shell, one end of the shell is provided with an air inlet communicating with one end of the cavity, and the other end of the shell is provided with an air outlet communicating with the other end of the cavity; an air inlet pipe set is arranged at the end, close to the air inlet, of the shell and comprises a center air inlet pipe extending in the axial direction and five peripheral air inlet pipes evenly distributed in the circumferential direction of the center air inlet pipe. The central air inlet pipe and the peripheral air inlet pipe form a bionic starfish type inlet structure for simulating a central disc and a radiation wrist structure of starfish; a plurality of spiral pieces arranged in the axial direction of the cavity are arranged in the cavity, and the arrangement angles of the adjacent spiral pieces are different. By means of the bionic starfish type inlet structure design, hydrogen is evenly dispersed to the whole mixing area, the mixing uniformity of natural gas and hydrogen is effectively improved, and meanwhile the risk of hydrogen embrittlement is delayed.

The reducing type pipeline natural gas hydrogen-doped mixer comprises a mixer main pipeline, the inlet end of the mixer main pipeline is provided with a reducing taper pipe section extending inwards, the small-diameter end of the reducing taper pipe section is communicated with a hole type injection pipe section, and a hydrogen conveying inlet pipeline is arranged on the side wall of the mixer main pipeline in a sealed and penetrating mode; an outlet of the hydrogen conveying inlet pipeline communicates with an injection hole of the hole type injection pipe section, and hydrogen enters the hole type injection pipe section through the hydrogen conveying inlet pipeline in a cross flow jet flow mode to be mixed with natural gas. A variable-diameter static mixer is further arranged in the mixer main pipeline, the small-diameter section of the variable-diameter static mixer can be inserted into the hole type injection pipe section, and the large-diameter section of the variable-diameter static mixer is arranged at the position, close to the outlet end, in the mixer main pipeline. The flow speed of natural gas is increased through the gradually-shrunk taper pipe section, jet flow acceleration of hydrogen is achieved through the hole type injection pipe section, kinetic energy of the natural gas and the hydrogen is fully utilized, and rapid, uniform and efficient mixing of hydrogen doped natural gas can be well achieved.

The invention relates to the technical field of flue gas desulfurization, and discloses a sintering flue gas desulfurization device which comprises a desulfurization tower, a flue gas inlet pipe is fixedly mounted on the desulfurization tower, a flue gas outlet pipe is fixedly mounted above the desulfurization tower, a base is fixedly mounted at the bottom of the desulfurization tower, and a purification assembly is arranged on the desulfurization tower. According to the sintering flue gas desulfurization device, in order to improve the desulfurization efficiency of the desulfurization device, the purification assembly is arranged and matched with the limestone slurry pipe on the desulfurization tower to convey slurry to the slurry conveying pipe, the spraying area of the limestone slurry is increased through the multiple sets of spraying pipes, and under the action of the spiral spoiler, flue gas guided in by the flue gas inlet pipe is discharged into the desulfurization tower through the flue gas inlet pipe. The demister is arranged below the flue gas outlet pipe, water mist in the desulfurized flue gas is effectively removed, and it is ensured that the discharged flue gas meets the standard.

Methods of manufacturing a substrate including a component, such as superabsorbent material, having a volatile hydrophobic coating are disclosed. The method can include providing a fluid supply including a liquid and providing a supply of the component. The component can include a volatile hydrophobic coating. The method can include introducing the component to the fluid supply. The method can also include transferring the component in the fluid supply to provide the substrate. The method can further include applying heat to the substrate. The heat can remove the volatile hydrophobic coating from the component.

The utility model discloses a multi-element gas automatic mixing device which comprises a plurality of gas branches, all the gas branches are jointly connected with a gas main path, the gas main path is connected with a mixing tank, the gas main path is provided with a static mixer, the mixing tank is provided with a dynamic mixer, and the static mixer is connected with the dynamic mixer. A gas outlet of the mixing tank is sequentially provided with a first-stage buffer tank, a second-stage buffer tank, a third-stage buffer tank and a first gas storage chamber in the gas conveying direction, and efficient mixing of gas is achieved through a static mixer and a dynamic mixer. The static mixer utilizes a spiral structure to generate rotation and turbulent flow to promote uniform mixing of gas; under the condition that the gas flow speed is lower or the gas types are more, the dynamic mixer is provided with an electric stirring blade, the mixing uniformity is further improved through mechanical stirring, the gas enters the buffer tank after being mixed through the arrangement of the multi-stage buffer tank, the pressure fluctuation is reduced, and the flow speed is homogenized. And the repeated diffusion and distribution process in the buffer tank improves the mixing uniformity of the gas.

The invention relates to the technical field of chemical equipment, in particular to an internal circulation esterification kettle which comprises a kettle body, a circulation stirring assembly, a driving assembly and a scraping assembly. A reaction cavity is formed in the kettle body; the circulating stirring assembly comprises a separation cylinder, a rotating shaft, a first paddle and a driving part; a circulation cavity is formed between the outer wall of the separation cylinder and the inner wall of the kettle body; the first paddle is arranged on the rotating shaft; the driving part is used for driving the rotating shaft to rotate; when the rotating shaft rotates, the first paddle can push materials from the first end of the separation barrel to the second end of the separation barrel, and then the materials flow back to the first end through the circulation cavity; the driving assembly comprises a first gear, a gear ring, a mounting frame and a second gear which form a planetary gear train; the scraping assembly comprises a reciprocating lead screw, a guide rod and a scraping plate, and when the rotating shaft rotates, the scraping plate can rotate by taking the central axis of the rotating shaft as the center and slide up and down along the inner wall of the kettle body in a reciprocating manner. The reaction kettle has the effects of improving the material mixing efficiency and uniformity and reducing adhesion between materials and the inner wall of the reaction kettle.

The invention discloses a gas mixing venturi tube and a bubble water device, and relates to the technical field of life electric appliances, the gas mixing venturi tube comprises a tube body, the tube body is provided with a main body part, and an inlet section, a gas suction section and an outlet section which are connected with the main body part; the main body part is provided with a contraction section, a throat pipe section and an expansion section, the inlet section is connected with the contraction section, and two ends of the expansion section are respectively connected with the throat pipe section and the outlet section; the main body part is further provided with an air cavity, and the air suction section is communicated with the throat pipe section through the air cavity. According to the gas mixing Venturi tube, the preparation efficiency and quality of bubble water can be improved, and the negative pressure stability of the throat tube section is improved.

The utility model relates to the technical field of carbon dioxide capture, in particular to a gas distributor and a carbon dioxide absorption tower. The gas distributor comprises an inner cylinder, a perforated plate and a guide plate group, a gas flow channel is formed between the outer peripheral surface of the inner cylinder and the inner peripheral surface of a tower body, and a gas inlet communicated with the gas flow channel is formed in the tower body; a plurality of through holes are formed in the perforated plate, and the perforated plate is connected to the top end of the inner cylinder; the two guide plate groups are symmetrically arranged on the two sides of the inner cylinder by taking the longitudinal axis section of the gas inlet as a symmetric plane; and each flow guide plate group comprises a plurality of flow guide plates which are distributed at intervals along the outer circumferential direction of the inner cylinder body. Smoke entering the gas flow channel can be divided into a plurality of gas flows through the two flow guide plate sets, the smoke is rapidly dispersed, meanwhile, gas and liquid can be separated in the downward flowing process of the gas flows, and therefore liquid drop entrainment is reduced; and a plurality of air flows are reflected upwards by the tower bottom, penetrate through the perforated plate and are further homogenized, so that uniformly distributed air flows are formed.

A static mixer includes a mixer housing, a mixing element including mixing bodies arranged one after another along a longitudinal axis so as to be capable of repeated separation and recombination of components, each of the mixing bodies including a first and second inlets, first and second lateral outlets and an intermediate outlet disposed between the first and the second lateral outlet, an input wall separating the first and second inlets, a deflection element arranged downstream of and adjacent to the input wall, first and second output walls arranged downstream of and adjacent to the deflection element, the first output wall separating the first lateral outlet and the intermediate outlet and the second output wall separating the intermediate outlet and the second lateral outlet.

The invention relates to the technical field of bubble generation, and provides a micro-nano bubble stable generation method and a micro-nano bubble stable generation device.The method comprises the steps that a liquid-phase working medium flows through a Venturi tube, so that negative pressure is formed in the throat portion of the Venturi tube, a gas-phase working medium is sucked in, preliminary mixing is conducted, and a gas-liquid mixture is obtained; the gas-liquid mixture is tangentially guided into a rotary-cut type excitation cavity to drive a free rotating impeller in the rotary-cut type excitation cavity to rotate, and fine shearing is conducted on bubbles; the gas-liquid mixture obtained after fine shearing is guided into a diffusion and flow stabilization cavity for speed reduction and flow stabilization; the gas-liquid mixture subjected to flow stabilization flows through a nanocrystallization foam stabilizing unit, a plurality of parallel micro-channels are arranged in the nanocrystallization foam stabilizing unit, and the surface of the inner wall of each micro-channel is covered with a layer of nanofiber net-shaped structure; and carrying out final nanocrystallization and interface stabilization treatment on the gas-liquid mixture through a nanofiber net structure, and outputting stable micro-nano bubble liquid. The problems of poor stability, short service life and high energy consumption of the traditional technology are solved.

The invention relates to the technical field of urea production, in particular to a urea production device. Comprising a mixing tank, a feeding hopper, a stirring device, a liquid inlet pipe and a liquid discharging pipe, an inner cylinder is arranged in the mixing tank and divides the mixing tank into an inner mixing bin for storing premixed liquid and an outer mixing bin for storing raw materials to be mixed from inside to outside, a filter screen plate is arranged above the inner cylinder, and small-particle raw materials are evenly dispersed in the inner mixing bin through the filter screen plate; and the large-particle raw materials are guided into the external mixing bin. In the liquid separation stage, water waves generated by vortex rotation are used for driving the floating plate to drive the drainage plate to float up and down in the premixed liquid, so that vortex outer ring solutions with different depths are guided to the axis, and the mixing degree of the solutions in the horizontal direction is enhanced; the floating plate is used for raising the vortex outer ring solution in an inclined manner, so that gravitational potential energy is used for impacting the rear part of the drainage plate, the local concentration difference is further broken, and the solution is promoted to reach a more uniform mixing state.

The invention provides a Venturi cavitator based on a rotational flow-pore plate coupling effect, and relates to the technical field of fluid cavitation, the Venturi cavitator comprises an inlet section, a throat part and an expansion section of a Venturi tube body, and a hollow spiral flow deflector is arranged on the inner wall of the inlet section. The spiral flow deflectors enable peripheral fluid close to the inner side wall surface to generate high-speed rotation, a stable rotation effect is formed, and a local low-pressure area is induced in the expansion section, so that pressure recovery caused by cavitation burst is effectively counteracted, the cavitation period interval is shortened, and the continuity of the cavitation process is enhanced; the hollow flow channel reorganizes and accelerates the fluid in the central area, the flow velocity of the throat is effectively improved, and the cavitation intensity is improved. The device is compact in structure and easy to manufacture, can improve cavitation intensity and continuity at the same time, is widely applicable to multiple fields such as sewage degradation, sterilization and disinfection, industrial emulsification, oil-water mixing treatment and the like, and has good application prospects and economic and social benefits.

The invention discloses a micropore bubbling aeration two-stage oscillation modulation synergistic system and an application method thereof. The modulation synergistic system comprises a two-stage oscillation device, an air supply unit connected to the upstream of the two-stage oscillation device, and a micropore coil pipe and an aeration tank which are connected to the downstream of the two-stage oscillation device. The two-stage oscillation device comprises a non-feedback oscillation cavity connected with the branch section, a sound wave oscillation cavity sequentially connected with the air inlet section, and a cavity connecting section connected with the non-feedback oscillation cavity and the sound wave oscillation cavity in parallel. Controlled pulsating oscillation airflow is injected into the microporous aeration system through the two-stage oscillation device, and periodic inertia force disturbance is introduced in the bubble generation stage; the pulsating pressure field breaks through gas-liquid interface force balance under traditional steady-state airflow, so that the bubble separation critical size is remarkably reduced, hole opening air film oscillation is accelerated through high-frequency pressure oscillation, necking fracture is promoted, and the bubble separation size is reduced; and meanwhile, transient shear force generated by the pulsating airflow inhibits interaction of adjacent bubble wake flows, and the coalescence probability is reduced.

The utility model discloses reaction equipment with high crude methyl ester yield, which comprises a stirring kettle and a material circulating system, the material circulating system comprises a circulating pump, a spray pipe arranged in the stirring kettle and a mixing nozzle arranged on the spray pipe, and a bottom outlet of the stirring kettle is connected with a feed port of the circulating pump through a first pipeline. An outlet of the circulating pump is connected with the spray pipe through a second pipeline; the mixing nozzle comprises a first sprayer and a second sprayer, and an outer flaring in the lower portion of the second sprayer is in clearance fit with the conical head through a connecting piece. The material circulating system can realize bottom-out and top-in of materials, so that the mixing of an oil phase and an enzyme water phase is promoted through the reciprocating circulation. In addition, the material circulating system is provided with a plurality of mixing nozzles, the flow speed of spraying of the first spray head is large, so that a negative pressure suction gap is formed at the joint of the second spray head and the first spray head, materials in the stirring kettle can enter the mixing nozzles under the action of negative pressure, an oil phase and an enzyme water phase are intensively mixed, and the yield of fatty acid methyl ester is improved.

The invention discloses a precise ammonia spraying system suitable for SNCR denitration, and relates to the technical field of ammonia spraying devices for SNCR denitration, the precise ammonia spraying system comprises a top cover fixedly mounted at the top of a boiler cyclone separator barrel, and a reciprocating pushing mechanism is mounted on the outer wall, located on the outer side of a spray gun, of the boiler cyclone separator barrel; and supporting cylinders which are distributed at equal intervals are fixed on the inner wall, close to the spray gun, of the boiler cyclone separator cylinder body. According to the precise ammonia spraying system suitable for SNCR denitration, the sleeve used for dispersing ammonia sprayed by the spray gun can rapidly rotate and transversely move, dead angles in the spraying process can be reduced, the ammonia is evenly distributed in the boiler cyclone separator barrel, mixing of the ammonia and flue gas is promoted, the working efficiency of the ammonia spraying system is improved, and the service life of the ammonia spraying system is prolonged. Moreover, the sleeve can generate slight vibration during rotation, dust particles in the through holes are vibrated off, the service life of the sleeve is prolonged, meanwhile, gas can be helped to form finer fog drops during spraying, ammonia gas can be better diffused conveniently, and the flue gas reaction efficiency is improved.

The invention provides a slurry preparation method and pulping equipment, and the slurry preparation method comprises the following steps: stirring and kneading materials in a kneading device to form primary kneaded slurry; conveying the primary kneaded slurry to a dispersing device for dispersing to obtain dispersed slurry; the dispersed slurry is circularly treated at least once between the dispersing device and the kneading device, so that the slurry is repeatedly kneaded and dispersed; and discharging the circularly treated slurry from the dispersing device to obtain the finished product slurry.

The invention relates to the field of petrochemical equipment, and discloses a cobweb-shaped oil-water emulsification turbulator with turbulent flow fins, which comprises an oil-water emulsification pipe, a cobweb-shaped turbulator arranged in the oil-water emulsification pipe, and annular fins and bent fins fixed on the inner side of the pipe wall of the oil-water emulsification pipe, the annular fins and the bent fins are distributed in the axial direction of the oil-water emulsification pipe, the bent fins are arranged close to the cobweb-shaped spoiler, and a gap for fluid circulation is formed between the bent fins and the cobweb-shaped spoiler. A multi-scale composite turbulent flow field is constructed through cooperative cooperation of the annular fins, the bent fins and the cobweb-shaped spoilers, the annular fins can effectively damage a boundary layer of a pipe wall and enhance local shear force, so that oil drops leaning against the wall are separated from the pipe wall and guided to a central area of a pipeline, and the bent fins further guide fluid to deviate towards the center so as to reduce flowing dead zones. The net-shaped structure of the cobweb-shaped spoiler is used for continuously stretching, shearing and secondarily crushing oil drops, and the oil-water mixing uniformity and the emulsifying efficiency are remarkably improved under the combined action of the three parts.

A pretreatment mixing and stirring device includes a cylindrical housing having a top plate, a bottom plate arranged to oppose to the top plate, a side plate arranged between the top plate and the bottom plate, and a mixing and stirring region where a calcined gypsum and an additive are mixed and stirred in an interior surrounded by the top plate, the bottom plate, and the side plate, a disk-shaped rotating plate arranged inside the housing, a rotating drive shaft, penetrating the top or bottom plate, and coupled to the rotating plate, a calcined gypsum supply port, arranged in the top plate, and supplying the calcined gypsum to the mixing and stirring region, and an additive supply port, arranged in at least one of the top and side plates, and supplying the additive to the mixing and stirring region.

The present invention discloses a commercial soda water intelligent mixing device, which specifically relates to the technical field of soda water preparation, and includes a bracket. The present invention provides a controller, a water pump, a soda water mixing nozzle, and a carbon dioxide inlet, so that water is pumped out through the water pump, and the original water flow is converted into water mist through the soda water mixing nozzle, and then carbon dioxide is introduced through the carbon dioxide inlet at the same time to react and generate soda water, so that the efficiency and effect of preparing soda water are better and the reaction of carbon dioxide and water is more complete. An evaluation coefficient of the device is established by collecting a water pressure difference coefficient, a water outlet deviation coefficient, and a power supply voltage instability coefficient, and the evaluation coefficient is compared with an evaluation coefficient threshold to determine whether the soda water prepared by the mixing device meets the merchant's expectations. If the evaluation coefficient is greater than the evaluation coefficient threshold, it is proved that the soda water produced by the mixing device at this time does not meet the merchant's expectations, and the working state of the mixing device needs to be stopped in time.

The invention discloses a membrane pore aeration ozone heterogeneous catalytic reactor and a water treatment system, and relates to the technical field of water treatment. The reactor comprises a reactor cavity, the top of the reactor cavity is provided with a water outlet assembly, and the bottom is provided with a water inlet assembly and a gas inlet assembly; the membrane component is arranged in the reactor cavity and comprises a bundle of hollow fiber membrane filaments which are bent in a U shape; the two ends of the hollow fiber membrane filaments are bundled and fixed in a mounting hard tube, the mounting hard tube is detachably connected with the air inlet assembly, and the air inlet assembly is used for communicating an external air supply device with the hollow fiber membrane filaments; micropores are distributed in the surfaces of the hollow fiber membrane filaments; and the reactor cavity is filled with catalyst particles. According to the membrane pore aeration ozone heterogeneous catalytic reactor provided by the invention, the ozone mass transfer efficiency and the utilization rate are improved, and the content of hydroxyl radicals used for degrading organic matters in water is increased, so that the organic matters which are difficult to degrade in water can be more effectively removed, and the ozone treatment operation cost is reduced.

A mixing section for an exhaust system of an internal combustion engine comprises a mixing section housing (16) through which exhaust gas (A) flows in a main exhaust gas flow direction (H), and a tubular mixing body (18) arranged in the mixing section housing (16) and extending in the direction of a longitudinal axis (L) of the mixing body, wherein the mixing body (18) defines a first flow volume (24) through which exhaust gas (A) flows radially outwards and defines a second flow volume (26) through which exhaust gas (A) flows radially inwards, wherein the mixing body (18) has a tubular first mixing body part (20) extending in the direction of the longitudinal axis (L) of the mixing body and at least one extension in the direction of the longitudinal axis of the mixing body on an outer surface (32) of the first mixing body part (20) facing the second flow volume (26) or on an inner surface (30) of the first mixing body part (20) facing the first flow volume (24). (L) extending,a tubular second mixing body part (34), wherein the second mixing body part (34) has a plurality of first projections (36) arranged adjacent to one another in the direction of the longitudinal axis (L) of the mixing body and in the circumferential direction around the longitudinal axis (L) of the mixing body and directed towards the first mixing body part (20), and wherein the second mixing body part (34) bears against the first mixing body part (20) in the region of at least a part of the first projections (36), preferably all of the first projections (36).

To provide a gas ejection nozzle which maintains high gas dissolution capacity by using a cavitation screw member and is also superior in self-priming capacity, and to provide a gas dissolution device and a gas dissolution method using the gas ejection nozzle.SOLUTION: A gas ejection nozzle 1 comprises: a nozzle body 2 in which a single liquid channel 11 having a liquid inlet 3 at one end and a liquid outlet 4 at the other end is formed, and in which a throttle part 9 is formed in the middle of the liquid channel 11 so as to have a smaller diameter than the liquid inlet 3; a cavitation screw member 10 disposed within the throttle part 9; and a gas dissolution diameter expansion part 13 which is connected to a downstream side of the throttle part 9 so as to form a part of the liquid channel 11, and which continuously or gradually expands an axial cross section toward the liquid outlet 4. A gas introduction hole 6 of the nozzle body 2 communicates with the throttle part 9 or the gas dissolution diameter expansion part 13 at a downstream side beyond all cavitation screw members 10 positioned within the throttle part 9, and is formed so as to connect an external part of the nozzle body 2 and the liquid path 11.SELECTED DRAWING: Figure 1

A system (10) for treating produce includes an application system (12) for applying a treatment liquid to the produce. A piston pump (20) is connected in liquid flow receiving communication with a source of treatment liquid (16), and also is connected in liquid flow expelling communication with an application line (18) leading to the application system. A control system (22) controls the operation of the piston pump to pump a selected dosage of the treatment liquid from the source of treatment liquid (16) to the application system (12).