75results about How to "Strengthen the degree of disturbance" patented technology

The invention discloses a novel oxygen enrichment tiny-oil ignition and ultralow load stable-combustion combustor. The novel oxygen enrichment tiny-oil ignition and ultralow load stable-combustion combustor comprises an oxygen enrichment guide pipe, a primary air pipe, a cylindrical oil-coal mixed combustion chamber, a secondary air pipe, a secondary air box and a pre-combustion chamber, wherein the central axes of the primary air pipe, the cylindrical oil-coal mixed combustion chamber, the secondary air pipe, the secondary air box and the pre-combustion chamber coincide. A secondary air inlet inclining in the circumferential direction is formed in the pipe wall of the secondary air box; the primary air pipe penetrates through the secondary air box in the axial direction, the oil-coal mixed combustion chamber is coaxially arranged in the primary air pipe, and a high-energy tiny-oil ignition oil gun and the oxygen enrichment guide pipe are arranged in the oil-coal mixed combustion chamber; the secondary air pipe with a rotational flow impeller is coaxially arranged outside the primary air pipe in a sleeved mode and an outlet end is provided with a bluff body; the pre-combustion chamber is arranged in the secondary air box, the inlet end of the pre-combustion chamber is provided with a graded air duct, and a plurality of disturbance air nozzles are installed in an outlet of the combustor. The ignition fuel saving ratio reaches over 90% and the novel oxygen enrichment tiny-oil ignition and ultralow load stable-combustion combustor has the function of low load stable combustion and the function of ultralow load stable combustion; the technologies of oxygen enrichment, coal dust concentration, graded air feeding and the like are adopted, so that the novel oxygen enrichment tiny-oil ignition and ultralow load stable-combustion combustor has the advantages of being high in coal dust burn-off rate, low in NOx discharge and the like.

The invention discloses a low-NOx pulverized coal burner, which comprises an inner secondary air box, a hierarchical air box and a disturbed air box. The inner secondary air box, the hierarchical air box and the disturbed air box are separated by a first clapboard and a second clapboard sequentially; the centers of the first clapboard and the second clapboard are provided with circular holes; each pipe wall of each of the three air boxes is correspondingly provided with an air inlet which inclines towards the circumferential direction; a primary air pipe axially passes through the inner secondary air box; an inner secondary air pipe with a swirl vane is coaxially sleeved outside the primary air pipe; the inner secondary air pipe is hermetically connected with the first clapboard; the inner secondary air pipe expands conicity and extends outwards to form a conical cylinder at the circular hole of the first clapboard; the conical cylinder is arranged in the hierarchical air box; the disturbed air box is coaxially provided with a precombustion chamber with two open ends; an annular channel is formed between the wall of the disturbed air box and the wall of the precombustion chamber; an annular end face is arranged at an outlet of the annular channel; a disturbed air nozzle is fixed at an opening of the annular end face; the inlet end of the precombustion chamber is hermetically connected with the second clapboard; an annular hierarchical air channel is formed at the root of the inlet of the precombustion chamber; and the conical cylinder is hermetically fixed with the inner wall of the hierarchical air channel.

This invention discloses a monomer shown in formula 1, wherein A is selected from formulae 2-4 or their combination; at least one of B and R is selected from alkyl, alkoxyl, ester group, formulae 5-8 or their combination; T is selected from O, N or their combination; X is selected from H, alkyl, halogen, cyano or their combination; n s a positive integer.

The invention discloses an internal recycle photoelectron-catalytic oxidation combined treatment device. According to the treatment device, a water inlet (2) is formed in the bottom of a treatment device cylinder (1) and is communicated with a circular water distributor (3); wastewater is uniformly distributed to the bottom of the device through the circular water distributor (3); a photoelectron-catalytic oxidation combined treatment system (4) is arranged above the circular water distributor (3); a sediment mud bucket (5) is arranged under the circular water distributor (3) and is communicated with a mud discharge hole (6); under the condition that a direct-current power supply is loaded to the photoelectron-catalytic oxidation combined treatment system (4), the wastewater is lifted to the top of the device from the bottom of a photoelectron-catalytic oxidation unit (7); part of the wastewater is discharged out from a water outlet (9) in the upper part of the device; another part of the wastewater is further circulated to the bottom of the photoelectron-catalytic oxidation unit (7) through a central partitioning cylinder (8) and is mixed with water, then circulation of the wastewater inside the photoelectron-catalytic oxidation combined treatment system (4) is achieved, mud dregs generated from reaction can be discharged out from the mud discharge hole (6) at regular time, and generated tail gases can be discharged out from a top tail gas treater (10).

The invention discloses a vortex broken flow type hydrogen cold box. The vortex broken flow type hydrogen cold box comprises an intercepting plate and a mixing box which are coaxially connected, wherein an annular gap is formed between the mixing box and a reactor cylinder body, a plurality of feeding inlets are uniformly formed in the bottom of the outer wall of the mixing box, an overflow cylinder is mounted on a gas-liquid mixture outlet in the center of the mixing box, the center height of the overflow cylinder is more than the height of the upper edge of each feeding inlet, the area of a gas-liquid inlet in the top end of the overflow cylinder is less than the sum of the areas of all feeding inlets, a plurality of broken flow holes are formed in the gas-liquid mixture outlet, and a plurality of guide plates of which the heads and the tails are connected in a staggered state and which are arranged in the shapes of circles are arranged around the overflow cylinder. According to the vortex broken flow type hydrogen cold box disclosed by the invention, the structure is simple, and the spiral guide plates, the overflow cylinder and the broken flow holes are arranged, so that a flat mixed structure is formed, under the condition of lowering the height of the hydrogen cold box, the gas-liquid two-phase mixed heat transfer effect is strengthened, and the problems of the existing hydrogen cold box such as short material residence time, insufficient mixing, nonuniform cooling, complex structure and big pressure drop can be effectively improved.

The invention provides a packing material combination plate element unsaturated evaporative radiator, which comprises a shell case, a fan, heat exchange elements, a spraying system and the like, wherein the lateral face of the case is provided with an air inlet and the top is provided with an air outlet, the air inlet of the case is provided with the heat exchange element, the spraying device is arranged above the heat exchange elements, the air outlet is provide with a draught fan, and a water baffle is arranged between the draught fan and the heat exchange elements. The heat exchange elements are formed by overlapping at least two groups of combination plate elements up and down, a polycarbonate asia ethyl ester packing material is filled between heat exchange plate pipes, the heat exchange plate pipes of two groups of up and down adjacent heat exchange elements are arranged in a staggering mode, the upper end of each heat exchange plate pipe is passed into a medium inlet pipe and is connected with a medium inlet header pipe, and the lower end of each heat exchange plate pipe is passed into a medium outlet pipe and is connected with a medium outlet header pipe; and water films are formed on the surfaces of the heat exchange elements under the action of the gravity of spray water, and the heat transfer is strengthened through water film evaporation. The packing material combination plate element unsaturated evaporative radiator achieves the crossed cross-flow type heat exchange between the water films and the air, and has high heat transfer efficiency, small wind resistance and perfect energy-saving and water-saving effect.

The invention relates to a membrane pollution vibration control device used in the process of treating algae containing water through a low-pressure spiral membrane and a method for controlling membrane pollution through the device. The device and the method aim at solving the problem that at present, no vibration control technology provided for the low-pressure spiral membrane pollution phenomenon is available. A vibration driver is arranged in the device, a spiral membrane reactor is driven by a drive motor to rotate along the axis, rotate back to the original position, reverse and rotate back to the original position, and therefore the vibration effect of a membrane assembly is achieved. According to the vibration method, the time when the spiral membrane maintains high-flux operation is prolonged, and the quality of effluent is guaranteed.

The invention relates to a device for fluidization loading or taking out a low-temperature protection agent for a biological tissue. The device is characterized by comprising a solution circulating module, a solution supplying module, a sample container, a temperature control box and a controller. The sample container is arranged in the temperature control box; the sample container is provided with a liquid inlet and a liquid outlet; the solution circulating module communicates with the liquid inlet and the liquid outlet of the sample container, so that a solution flows through the sample container in a circulating way; the solution supply module communicates with the solution circulating module so as to supply the solution to the solution circulating module; the controller is respectively and electrically connected with the solution supplying module, the solution circulating module and the temperature control box. According to the automation device, the threshold treatment temperature can be reduced, and meanwhile, the speed rate for loading and taking the low-temperature protection agent in and out of the biological tissue is accelerated.

The invention provides a high efficiency structured packing, which includes a packing layer main body and packing sections. The high efficiency structured packing is characterized in that: the packingcomprises bevel edge packing, straight edge packing and openings, the packing layer main body consists of several packing sections, each packing section consists of bevel edge packing and straight edge packing, the top and bottom of the bevel edge packing are respectively provided with a section of straight edge packing, and the bevel edge packing is equipped with a plurality of openings. Compared with the prior art, the high efficiency structured packing provided by the invention is reasonable in structure, the straight edge packing makes the vapor-liquid phase flow channel between two adjacent packing layers smoother, and reduces the circulation resistance drop of vapor-liquid two phases; the opening rate is appropriately increased, thus making the two side areas wet and vapor-liquid contact exchange fuller, and effectively improving the utilization rate of the specific surface area of the packing; the alternate combination structure of straight edge ripples and inclined ripples enhances the disturbance degree of vapor-liquid phases, improves the driving force of mass transfer, and reduces the resistance of mass transfer, thereby further improving the treatment capacity and masstransfer efficiency.

The invention discloses a heat exchanger for waste heat recovery of a coal-fired boiler. The design concept combining a section-separated heat transfer enhancement principle and a technology for flexibly adjusting the tube wall temperature through graded water supply is adopted, the heat exchanger is divided into a high-temperature section adopting carbon steel and a low-temperature section adopting ND steel, tube bundles are staggered, media inside and outside tubes are in a counter-flow type, the tube wall temperature of the high-temperature section and the low-temperature section is adjusted precisely in a graded water supply manner, so that the tube wall temperature is higher than the acid dew point temperature of flue gas throughout, and a low-temperature corrosion relieving effect is realized. The technical problems of low heat transfer temperature pressure and serious low-temperature acid-dew-point corrosion in low-temperature flue gas waste heat recovery of the coal-fired boiler are solved very well, by means of combination of section-separated heat transfer enhancement and flexible adjustment of the tube wall temperature through graded water supply, the heat exchange performance and the anti-corrosion effect of the low-temperature heat exchanger are improved obviously, the efficiency and the economical efficiency of the low-temperature flue gas waste heat recovery of the coal-fired boiler are improved substantially, and the heat exchanger has good social and economic benefit and great industrial application and popularization potential.

The invention discloses a production method of Luzhou-flavor liquor and a steaming kettle applied to the method, relates to the field of liquor production. The production method of the Luzhou-flavor liquor comprises the following steps: S1, preparing a prefabricated material; S2, preparing auxiliary materials; S3, performing auxiliary material treatment; S4, blending the ingredients; S5, performing steaming in a steamer; S6, steaming grains; S7, discharging from the steamer; S8, performing ventilation and grain stillage cooling; S9, preparing powder of yeast for making hard liquor; S10, performing yeast mixing; S11, performing fermenting in a tank; and S12, distilling the prefabricated fermented grains, namely adding the prefabricated fermented grains into a steamer pot for distilling, distilling off raw wine to obtain fermented grains, discarding a part of the fermented grains, and adding the rest of the fermented grains into the step S4 for recycling. Due to the fact that the steaming kettle is adopted for steaming the rice hulls, the amount of furfural generated in the rice hulls is reduced, and the influence of furfural in the rice hulls on the quality of white spirit is reduced; and the invention further provides the steaming kettle which has the effect of improving the material heating uniformity.

The invention discloses a method and a device for separate oxidation and cyclone purification of organic waste gas. The device comprises a cyclone purifying tower and a catalytic absorbent recycling system arranged at the bottom of the cyclone purifying tower, wherein a catalytic absorbent cyclone atomizing layer, an ultraviolet separate oxidation layer and an absorbed waste gas demisting layer are sequentially arranged in the cyclone purifying tower from bottom to top; the catalytic absorbent recycling system is used for providing a nano-titania atomization liquid required for atomization for the catalytic absorbent cyclone atomizing layer and recycling the nano-titania slurry falling to the catalytic absorbent recycling system under the action of gravity. Cyclone atomizers are adopted for atomizing the nano-titania slurry, the contact area of the nano-titania slurry and organic waste gas is increased, and the catalytic efficiency is improved; the cyclone atomizers are arranged in a tangent circle manner, so that the nano-titania slurry spirally rises along the tangent circle, the disturbing degree of the organic waste gas and a catalyst is improved, and the reaction rate is increased.

The invention discloses a welding plate heat exchanger. The welding plate heat exchanger comprises a shell and a heat exchange plate set inside the shell; the shell is rectangular and horizontally arranged; large half round channels are arranged at the two ends of the shell; the top of one of the large half round channels is provided with a cooled medium inlet; the top of the other large half round channel is provided with a cooled medium outlet; a small half round channel is arranged on the shell wall of the upper side, close to the cooled medium inlet, of the shell; the top of the small halfround channel is provided with a cooling medium outlet; a small half round channel is arranged on the shell wall of the lower side, close to the cooled medium outlet, of the shell; the top of the small half round channel is provided with a cooling medium inlet; the heat exchange plate set is formed by overlapping a plurality of heat exchange plate pair layer by layer; and each heat exchange platepair comprises an upper heat exchange plate and a lower heat exchange plate which are opposite. The effects that the welding plate heat exchanger can bear high temperature, is resistant to corrosion,high in intensity, not prone to deforming, not prone to being blocked and high in heat exchange efficiency can be achieved.

The invention discloses a continuous self-cleaning oil-water separation device. The device is mainly composed of a supporting frame, a liquid inlet pipe, flanges, a coating material, a flow dividing pipe, a valve, multi-stage structure absorption cotton, a liquid draining pipe, a separation liquid collecting box, a stainless steel net, a fluid driving rotor, a steel wire rope, a position sensor, acontroller, an electromagnetic limiting device and a fixing piece. The stainless steel net is produced to be barrel-shaped to be matched with the flanges, the two ends of the stainless steel net arewelded with the flanges and connected with the liquid inlet pipe and the flow dividing pipe respectively, the outside of the stainless steel net is coated with the coating material with the certain thickness and the certain strength, the separation liquid collecting box is placed on the lower face, and the fluid driving rotor is arranged in the stainless steel net. The device achieves self-cleaning by internally arranging the fluid driving rotor, the separation precision is improved through secondary separation conducted by the rear-arranged multi-stage structure absorption cotton, macroporesat the front end can further contain impurity particles in the oil-water separation liquid, the separation liquid is purified particularly, the post-treatment difficulty of the separation liquid is simplified, and the service life of the absorption cotton is prolonged.

The invention relates to a novel 900-t/d high-heat-value domestic garbage incinerator. The incinerator is characterized in that a hearth is 4.5-8m in the width; the incinerator comprises a fire grate(1) at the bottom of the hearth, a feed inlet (2) at the front end, a slag outlet (3) at the tail end, fire-resistant furnace walls (8) at two sides of the fire grate, a hearth wall front arch (4) atthe upper part of the hearth, two ignition burners (6) at the upper part of the hearth; left and a right side walls (9), an auxiliary burner (7), a first flue inlet (10) at the front middle part of the hearth, a secondary air pipe (11) at the lower part of the first flue, and water-cooled walls arranged on the first flue (10), the front arch (4), a rear arch (5) and the side walls (9). The incinerator is suitable for the incineration treatment of high-heat value domestic garbage, and has the advantages of wide working condition adaptability, long service life of a boiler, low failure rate, high combustion efficiency, low pollutant discharge and the like.

The invention discloses a low-temperature-corrosion-resistant smoke waste heat exchanger and belongs to the fields of smoke waste heat utilization and low-temperature-corrosion-resistant design. The low-temperature-corrosion-resistant smoke waste heat exchanger comprises a shell and finned tubes; the upper part of the shell is provided with a water outlet header, and the lower part of the shell is provided with a water inlet header; and straight tube sections of the finned tubes are arranged in the shell, bent tube sections of the finned tubes extend out of the shell, grooves are formed in the bottoms of the straight tube sections of the finned tubes, and a plurality of smoke flow guide blocks are densely distributed among the straight tube sections of every two adjacent finned tubes and along the axial directions of the finned tubes. The thermal stress and structural strength are calculated to meet the requirement of a project, in addition, the heat exchange efficiency can be increased to a certain extent, and the low-temperature-corrosion-resistant smoke waste heat exchanger has an obvious industrial application value.