348results about How to "Improve burnout rate" 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 an oxygen-enriched combustion method of a lignite methyl alcohol coal slurry fuel material in a compression-type internal combustion engine. The problem of difficulty in ignition of the traditional water coal slurry in the internal combustion engine is solved by utilizing the methyl alcohol coal slurry and oxygen-enriched combustion technology; and zero carbon emission of the whole system is realized through collecting CO2 generated by tail gas, and the pollution to environment is eliminated. The method provided by the invention adopts the following technical scheme which comprises the following steps of: taking ultra-fine ultra-clean ignite methyl alcohol coal slurry as a fuel material; taking pure oxygen and CO2 mixed gas with high concentration in recycled tail gas as a combustion-supporting gas; and carrying out enriched-oxygen combustion in the compression-type internal combustion engine, and generating a driving force by the compression-type internal combustion engine. Combustion is carried out by adopting pure oxygen and the recycled CO2 in the tail gas of the internal combustion engine as the combustion-supporting gas, the formation of NOX in the tail gas is reduced effectively, the concentration of CO2 in the tail gas is improved, the tail gas treatment expense is reduced, and the treated tail gas is easy to compress and store. The combustion method is suitable for a distribution-type power generation system and a large ship motive power system.

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.

The invention relates to a storage-type super-low nitric oxide system in a coal fired boiler coal mill. On the basis of the existing low-nitrogen burning technology, the superfine coal powder preparation technology and the smoke circulating technology are adopted. The smoke circulating technology adopts cold furnace smoke to be mixed with primary air to be supercharged by a primary fan, the heating and powder feeding technology of an air preheater and the hot air and high-temperature furnace smoke drying technology of the powder production system are adopted, i.e. superfine coal powder can be prepared, the hot furnace smoke enters a primary air large air bellow, the hot furnace smoke is mixed with superfine coal powder prepared by a superfine coal powder preparation device in a coal powder blender and supplied by a powder supply machine from a coal powder cabin to be heated, and the air-powder mixture is fed into a low-nitrogen burner through a primary air pipe. In the main burning area of the boiler, since the air content of the furnace smoke is little, a lower residual air coefficient can be realized, the emission of the nitric oxide can be reduced.

The invention provides a fire coal efficient catalysis combustion-supporting agent and a preparation method and use method thereof. The combustion-supporting agent provided by the invention comprises the following components in parts by weight: 20-40 parts of basic copper carbonate, 10-25 parts of calcium oxide, 5-20 parts of citric acid, 5-10 parts of ammonium metavanadate, 5-10 parts of urea, 5-10 parts of potassium carbonate and 5-10 parts of borax. The combustion-supporting agent can also contain 5-10 parts of lanthanide oxide, 5-15 parts of magnesium powder and 0-10 parts of iron nitrate. The invention has the following beneficial effects: the components of the combined combustion-supporting agent release or transfer active oxygen at the high temperature; the macromolecular structures of coal are damaged to break the bridge bonds between the connecting structure units, improve the combustibility of fire coal and increase the burn-off rate of coal, thus fire coal can be fully utilized and the aim of energy saving can be achieved; and the combustion-supporting agent performs combination reactions with the combustion products of coal such as SO2 and the generated solids which are difficult to volatilize enter ash, thus the emissions of gaseous pollutants can be reduced.

The invention discloses a pulse-combustion control method of a steel rolling heating furnace, namely at least four gas nozzles are arranged at the two sides of the heating furnace and located at the upper and lower parts of blanks in the blank along the length direction of the oven, thus whole-side-burning is formed for the heating furnace, the pulse of opening and closing of the whole gas nozzles is finished in T time and T is taken as a cycle period, each gas nozzle is opened at Ts interval successively, the quantity of the gas nozzles is N, thus in a pulse cycle period Ts=T/N, each gas nozzle open pulse order is set as required and opened by rated heating efficiency, each gas nozzle open pulse time is T1, T2...TQ, and the each gas nozzle open pulse time T1, T2... and TQ are calculated by the PID controller of the heating furnace control system according to the set value and the measured value of the furnace temperature. The pulse-combustion control method provided by the invention has the advantages of improving the furnace-shape, balancing the workload of the gas nozzle, improving fuel burn-off rate, strengthening the heat transfer efficiency of the blank, saving the fuel loss and improving control accuracy and flexibility of the furnace temperature, and is convenient in maintain and operation.

The invention provides a system for reducing boiler NOx emission by tertiary air concentrated-diluted separation. An outlet of a tertiary air powder exhaust fan is connected with a coal powder concentrated-diluted separator; a separation blade for adjusting a separation quantity of concentrated-diluted coal powder is arranged on an inlet section of the coal powder concentrated-diluted separator, and a concentrated coal powder pipe and a diluted coal powder pipe are arranged on an outlet section; the concentrated coal powder pipe is connected with at least one layer of hearth main combustion area middle lower nozzles; and the diluted coal powder pipe is connected with at least one layer of hearth main combustion area upper nozzles. The invention further provides a method for reducing boiler NOx emission by tertiary air concentrated-diluted separation; tertiary air containing thin coal powder is separated as concentrated and diluted two parts of coal powder air currents; and the concentrated and diluted two parts of coal powder air currents are respectively sprayed into the middle lower part and the upper part of a hearth main combustion area. The concentrated coal powder current replaces one part of secondary air to form an oxygen debt environment in the main combustion area so as to enhance the reducibility of the main combustion area; the diluted coal powder current is quickly burnt to consume oxygen so as to enhance the reducibility of NOx in a boiler; and the secondary air quantity reduced in the main combustion area is replenished to high-level burnt air so as to guarantee the burn-off rate of the coal powder in the boiler.

The invention provides a method for preparing biomass moulded coal by using biomass and inferior smokeless pulverized coal as raw materials. The biomass moulded coal is prepared by uniformly mixing the biomass, the inferior smokeless pulverized coal and additives (a sulfur fixation agent, a biomass binder, an oxidant and a waterproofing agent), and performing low-pressure compression moulding by a wet method, wherein the sulfur fixation agent is calcined lime CaO; the biomass binder is light yellow dope prepared by treating bagasse by using 1 to 2 percent sodium hydroxide solution; the oxidant is potassium permanganate; and the waterproofing agent is tar or a binder. The biomass moulded coal comprises following raw materials in part by mass: 40 to 65 parts of inferior smokeless pulverized coal, 25 to 55 parts of biomass and 5 to 10 parts of additive. The biomass moulded coal has the advantages of low cost, low ignition point, high burn-off rate and integrative desulfurization and water proofing performance, and has great significance of energy conservation and environmental protection.

A resource utilization method of paint slag includes the following steps that (1) pretreatment and separation are conducted, specifically, the wet paint slag is pretreated through a grinding modified spray drying method and separated into two components which are powdery or granular slag and organic matter waster liquid, or the wet paint slag is pretreated and separated into two components which are solid slag and organic matter waster liquid through an acid-modified baking hardening treatment technology; and (2) the water-containing organic matter waster liquid obtained in the step (1) is placed in a stirring tank, an emulsifying agent and a modifier are sequentially added into the water-containing organic matter waster liquid with constant stirring, uniform stirring is conducted, and a product is obtained. According to component characteristics of the wet paint slag, the wet paint slag is pretreated and separated into the two components which are the solid slag raw material convenient to use and the organic matter waster liquid containing volatile matter, namely water, and then the water-containing organic matter waster liquid is made into the liquid-state coal clean combustion improver; and the process method is simple, safe and free of secondary pollution, takes effect rapidly, is low in treatment or utilization cost, and is good in economical efficiency.

The invention discloses a plasma oil-free ignition combustor. The plasma oil-free ignition combustor comprises a plasma generator and a combustor, wherein an annular oxygen sleeve for supplementing oxygen to support combustion is arranged outside the plasma generator; the plasma generator and the sleeve are arranged coaxially; and the annular oxygen sleeve is connected with an oxygen pipeline. Because the annular oxygen sleeve is connected with the oxygen pipeline, the oxygen can enter the combustor through the annular oxygen sleeve, a local oxygen-enriched area is formed in the combustor and in a space of flowing pulverized coal airflow in a boiler, and combustion of the pulverized coal airflow can be intensified.

The invention provides a multistage hydraulic mechanical garbage incinerator and a control method for the same. The multistage hydraulic mechanical garbage incinerator comprises a feeding port, a feeding fire grate, an incinerating fire grate, a primary air supply system and a secondary air supply system. The incinerating fire grate is longitudinally divided into five units, wherein the first unit, the second unit, the third unit and the fourth unit are standard units, the fifth unit is a tail end lengthened unit, each unit comprises a plurality of sliding fire grate segments, turning fire grate segments and fixed fire grate segments, and the incinerating fire grate is integrally and longitudinally divided into a drying section, a burning section and a burnout section by the five units. The multistage hydraulic mechanical garbage incinerator is characterized in that the fire grate segments in each row of the incinerating fire grate are transversely driven by a shaft and transversely supported by a steel frame at three positions at the least. By the aid of the multistage hydraulic mechanical garbage incinerator, the shortcomings of an existing garbage incinerator are improved, and burnout ratio of garbage incineration is increased.

The application discloses a control system for optimized combustion of a combustor. The system comprises a gas component detection unit, an optimized control device and a secondary air executing device, wherein the gas component detection unit is used for detecting smoke component numerical values of a region where the combustor is and of a region of a rear flue of a boiler and sending the detection result to the optimized control device; the optimized control device is connected to the gas component detection unit for receiving the smoke component numerical values detected by the gas component detection unit and generating a control command according to the smoke component numerical values; the secondary air executing device is connected to the optimized control device for receiving the control command sent by the optimized control device and controlling a second air baffle plate executing mechanism according to the control command. According to the technical scheme disclosed by the invention, operation under a relatively low excessive air coefficient is guaranteed by controlling the air supply amount of the combustor, so that the burnout efficiency of fuels is effectively improved, the reducing atmosphere of the boiler is reduced and coking and corroding phenomena are improved while the heat loss due to exhaust gas is reduced, and the combustion process is safe, efficient and low in pollution.

The invention relates to an ejecting staged combustion W flame boiler for improving ignition and combustion of pulverized coal. The W flame boiler comprises a furnace hearth which is formed by an upper furnace hearth, a lower furnace hearth, a front furnace arch and a rear furnace arch, a plurality of secondary air nozzle groups which are arranged on the front furnace arch and the rear furnace arch, and a plurality of pulverized coal airflow nozzle groups, wherein the plurality of secondary air nozzle groups and the plurality of pulverized coal airflow nozzle groups are arranged side by side linearly, equidistantly and abreast along a width direction of a furnace, the plurality of pulverized coal airflow nozzle groups can be arranged on the furnace arches at fixed angles, an incident angle of secondary air can be adjusted, a plurality of over-fire air nozzles with adjustable incident angles can be formed in the upper furnace hearth, and two layers of tertiary air nozzles with the adjustable incident angles can be formed in water-cooled walls of front and rear walls of each furnace hearth. By adopting the W flame boiler disclosed by the invention, the combustion of the pulverized coal in the furnace can be effectively improved, the adaptive capacity of the boiler to coal types can be improved, the heat and reheat steam temperature can be effectively adjusted to reach a design value, the emission of NOx and the flue gas temperature can be reduced, slag bonding of the front and rear walls can be prevented, and the thermal fatigue existing in water-cooled walls of a combustion chamber hopper can be avoided.

The invention discloses a spiral-flow type fluidized bed incinerator which comprises an incinerator body and a cyclone separator. The incinerator body is used for providing combustion space for a fluidized bed, and the cyclone separator is used for recycling insufficiently-combusted ingredients for secondary combustion. At least three layers of secondary air jet orifices are further formed in the walls of the incinerator body and located in a transition zone between a dense-phase zone and a lean-phase zone. The other ends of the secondary air jet orifices are communicated with a secondary air source. The secondary air jet orifices on the same layer are distributed in the walls of the incinerator body. The air flow is spiral so as to enhance transverse mixing of particles and air in the incinerator body and prolong the residence time of the particles in the incinerator body. High-speed secondary air is jetted into the lean-phase zone on the upper portion of an air distribution plate of the circulation fluidized bed incinerator body in a classified manner through wall type tangential firing, so that transverse mixing of particles and air is enhanced, temperature distribution in different areas in the dense-phase zone is more uniform, the combustion efficiency and the desulphurization efficiency are improved, NOx emissions are lowered, the heat transferring is enhanced, and the equipment size is reduced.

The invention relates to an ash internal cycle fluid afterburning device, based on high-temperature separation, wherein the invention uses furnace and secondary wind to realize initial high-temperature separation and sets high-temperature combined water cooling separator at the heated surface of water condense slag tube beam at the outlet of high-temperature smoke to realize ash high-temperature separation; and the separated ash is feedback to the high-temperature area to be cycle fluidized burnt, to meet the burning conditions as temperature, time, and disturbing mixing, to improve the burning rate and reduce the pollution. The invention can improve the burnt rate and the burning efficiency of coal.

The invention discloses a torch combustion system with automatically adjustable sound speed. The torch combustion system comprises a torch combustor (14), a torch header pipe (12), torch branch pipes (13), a quincuncial flame holder (15) and a vibration attenuation support (16), wherein the torch combustor (14) is installed on the torch branch pipes (13), air inlets of the torch branch pipes (13) are all connected with the torch header pipe (12), the quincuncial flame holder (15) and the torch branch pipes (13) are connected to form an integral structure through the vibration attenuation support (16). The torch combustion system is characterized in that the torch combustor (14) comprises a flow guide cover (11), an external sleeve (7) and a supporting bar (9), the flow guide cover is installed at the upper end of the supporting bar, the external sleeve is sleeved on the supporting bar, and the lower end of the supporting bar is connected with a device for automatically adjusting the height of the flow guide cover (11). According to the torch combustion system, the structure is simple, the size of an air outlet can be automatically adjusted according to the pressure of flare gas, the combustion effect can be obviously improved and the combustion efficiency is high.

The invention relates to a magnetic electrode small-particle-size hydroxide ion generator. The magnetic electrode small-particle-size hydroxide ion generator comprises a raw material air supply channel, a cathode insulation fixation plate, a tunnel cylinder and an anode insulation fixation plate, wherein the cathode insulation fixation plate, the tunnel cylinder and the anode insulation fixation plate form a sealing cavity, the raw material air supply channel passes through the cathode insulation fixation plate and communicates with a cathode selection network inside the tunnel cylinder through a cathode conductive ring, the other end of the cathode selection network is connected with one end of an anode selection network, the other end of the anode selection network is fixed on the anode insulation fixation plate, an anode discharge needle is also fixed on the anode insulation fixation plate, the anode discharge needle is connected with a pulse high-frequency discharger, and the top portion of the tunnel cylinder is provided with a hydroxide ion air channel. Small-particle-size air negative ions prepared by use of the generator are widely applied, and since a prepared gas contains numerous negative hydrogen, oxygen ions and free electrons and is segmented and magnetized into small particle sizes, the magnetic electrode small-particle-size hydroxide ion generator can be widely applied to a health care industry, a medical industry and industrial combustion and machine combustion industries.

Disclosed is a secondary air offset whirl pulverized coal burner for a W flame boiler. The problems of high NOx discharge amount, high fly ash combustible matter content, slag-bonding to water walls of front and back walls of a lower combustion chamber and high temperature corrosion of the W flame boiler which is provided with an existing whirl pulverized coal burner on an arch are solved. A circular ring inner secondary air stop block in the circumferential direction is added in inner secondary air on a dividing cylinder of primary air and inner secondary air of the whirl pulverized coal burner; the angle of the circular ring inner secondary air stop block in the circumferential direction is 180 degrees; a circular ring outer secondary air stop block in the circumferential direction is added in outer secondary air on a dividing cylinder of the inner secondary air and the outer secondary air; the angle of the circular ring outer secondary air stop block in the circumferential direction is 180 degrees; the boundary line in the diameter direction of the circular ring inner secondary air stop block and the circular ring outer secondary air stop block is parallel to the front and back walls of the boiler; the circular ring inner secondary air stop block and the circular ring outer secondary air stop block are mounted on one side close to the center of a combustion chamber. The secondary air offset whirl pulverized coal burner is used for the W flame boiler.