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83results about How to "Increase cycle ratio" patented technology

Fine coal pressurization dense phase transporting bed gasification method and device

A pulverized coal pressure dense transport bed gasification method and installation of the invention relates to gasification technology and employs in-furnace desulfurization craft. Pulverized coal and desulfurizer are sent into gasification furnace through the middle and lower part of gasification furnace by a feeder, and then react with a gasifying agent. Reaction mass flow upward from the bottom of the gasification furnace, and enter into a multistage gas-solid separator from an export on the top of the gasification furnace. Most solids are separated in the gas-solid separator and enter into the low part of the gasification furnace by a high flux return feeder to continue to participate in reaction. Gas products with a small amount of solid enter into a gas cooler which can recover gas manifested heat to generate steam. The enter modes of the gasifying agent are bottom once wind and cyclone twice wind, otherwise, the reactor can also be use to burn. Because of the high-rate cycle, high solid content and high gas-solid mixing in the gasification furnace of the invention, the gasification strength and gasification rate of the gasification furnace can be improved and higher gasification efficiency and carbon conversion rate can be obtained.
Owner:INST OF ENGINEERING THERMOPHYSICS - CHINESE ACAD OF SCI

Device for improving pipe and gas-solid circumfluence bed coupling reaction

The invention provides a lift pipe and air-solid circulation bed coupling reaction device which at least includes a lift pipe, a shower head distributor, a guide cylinder, an annular space air distribution ring, an outer cylinder, an inner circulation pipe, an outer circulation fluidized bed, an outer circulation pipe and an air-solid separating system. Particles and air are transmitted upwards along the lift pipe, pass through the shower head distributor and enter the upper annular fluidized bed to form a central air lifting type circumfluence between the guide cylinder and the annular space. Part of the particles below the outer cylinder enters the lift pipe through the inner circulation pipe and another part enters the outer circulation fluidized bed to be mixed with the original particles in the outer circulation fluidized bed; the mixed particles enter the lift pipe through the outer circulation pipe; the positions where the inner circulation pipe and the outer circulation pipe enter the lift pipe can be flexibly arranged; the lift pipe and air-solid circulation bed coupling reaction device overcomes the limitations of system pressure balance and short reaction time and has the advantages that each area is flexible to be operated and controlled, the air-solid contact efficiency of the annular fluidized bed is high and the resistance above the distributor is small, etc. The device can be broadly applied to the fields of energy supply, chemical industries and particle combustion, etc.
Owner:CHINA UNIV OF PETROLEUM (BEIJING)

Coal gas washing, dedusting and purifying process

The invention relates to a coal gas washing process, in particular to a coal gas washing, dedusting and purifying process. The process can solve the problems of non-complete dedusting and non-complete purification of the traditional coal gas washing process. The coal gas washing, dedusting and purifying process is realized by adopting the following steps: a) introducing coal gas containing dust into a dedusting and washing tower; b) leading waste water after dedusting and washing to flow into a sedimentation tank for sedimentation via the tower bottom of the dedusting and washing tower; c) leading the coal gas after washing to enter into a purifying and washing tower, thereby being in countercurrent contact with circulating water at the upper part of the purifying and washing tower for washing and then further being in countercurrent contact with desalted water at the tower top of the purifying and washing tower for further washing and purifying; and d) leading the water after purifying and washing to flow into a circulating tank via the tower bottom of the purifying and washing tower and then leading the water to be divided into two lines. The coal gas washing, dedusting and purifying process can effectively solve the problems of non-complete dedusting and non-complete purification of the traditional coal gas washing process and is suitable for coal gas washing during the coal gas making process.
Owner:SHANXI JINCHENG ANTHRACITE COAL MINING GRP CO LTD

Low-nitrogen combustion technique based on circulating fluidized bed boiler

ActiveCN106051749ASolve the reduction of NOx emissionsSolve the high carbon content of fly ashFluidized bed combustionFluegas recirculationBurning outCirculating fluidized bed boiler
The invention discloses a low-nitrogen combustion technique based on circulating fluidized bed boiler. The circulating fluidized bed boiler comprises a boiler body, a cyclone separator, a deduster, an induced draft fan, a primary air supply system and a secondary air supply system which are connected in sequence. A smoke recirculation pipe is drawn out behind the induced draft fan. The primary air supply system and the secondary air supply system are connected to the smoke recirculation pipe in parallel. A burn-out chamber is arranged at an outlet of the cyclone separator. The low-nitrogen combustion technique based on the circulating fluidized bed boiler comprises the following steps that pulverized coal enters the boiler body under the action of primary air, specifically, the amount of smoke recirculation air in the primary air accounts for 8-10% the total air amount of the primary amount, and the amount of the primary air accounts for 40-45% of the total air amount; secondary air is introduced into the boiler body through the secondary air supply system, specifically, the amount of smoke recirculation air in the secondary air accounts for 12-14% the total air amount of the secondary air; fine flying ash enters the burn-out chamber; and over fire air is introduced into the burn-out chamber. According to the low-nitrogen combustion technique based on the circulating fluidized bed boiler, the burn-out chamber is arranged at the outlet of the separator, and part of smoke is mixed into the primary air and the secondary air, so that generation of NOx is reduced.
Owner:QINGDAO JINTIAN THERMAL POWER CO LTD

Method for separating CO2 through chemical looping combustion in coal pressure high-density circulating fluidized bed

ActiveCN102183014AIncrease the combustion reaction rateSolving the Response Matching ProblemFluidized bed combustionIndirect carbon-dioxide mitigationCycloneHigh density
The invention provides a method for separating CO2 through chemical looping combustion in a coal pressure high-density circulating fluidized bed, which comprises the following steps: coal particles and a gasifying agent are subjected to gasification reaction in a fuel reactor 1 of the coal pressure high-density circulating fluidized bed, and gasified products and oxygen carriers which return to the fuel reactor are subjected to combustion reaction to produce CO2 and H2O; smoke which is produced during the reaction and carries oxygen-lost oxygen carriers and carbon-containing coal ash enters a primary cyclone separator 2 for separation, and separated oxygen-lost oxygen carriers are in contact with transversely passing air for reaction in an air reactor 5 of a cross flow moving bed to be regenerated and are turned to the combustion reactor through a primary material returning device 8 to continuously participate in the combustion reaction; and separated smoke in the primary cyclone separator 2 further enters a secondary cyclone separator 10 for separation, solid particles secondarily separated are returned to the fuel reactor 1 through a secondary material returning device 13 to continuously participate in the combustion reaction, and H2O is removed from the separated gases through condensation to obtain high-purity CO2.
Owner:SOUTHEAST UNIV

Apparatus for converting tar component and carbonaceous particles in raw gas, and method thereof

The invention relates to an apparatus for converting a tar component and carbonaceous particles in raw gas, and a method thereof. The conversion apparatus comprises a conversion system, a material return system and a material sealing system. The conversion system is mainly composed of a solid particle distribution zone, a partial oxidation zone and an advanced treatment zone. The material return system is composed of a gas-solid shunting device, a solid particle trapping device and a vertical dipleg. The material sealing system is composed of a seal level control device, an annular seal and a material return inclined tube. A partial oxidation reduction reaction of a gasification agent, and the tar component and carbonaceous particles carried in the raw gas is carried out to convert the tar component and the carbonaceous particles into gas, so the advanced conversion treatment of the tar component and the carbonaceous particles in the raw gas is realized, and the energy conversion efficiency is greatly improved. The apparatus and the method have the technical advantages of simple operation process, low apparatus investment and running cost, high conversion rate and the like.
Owner:陕西延长石油(集团)有限责任公司碳氢高效利用技术研究中心

Circulating fluidized bed boiler system for achieving low nitrogen oxide discharge

InactiveCN105805730AImprove fluidization characteristicsWell mixedFluidized bed combustionStaged combustionFlue gasEngineering
The invention discloses a circulating fluidized bed boiler system for achieving low nitrogen oxide discharge. The circulating fluidized bed boiler system comprises a boiler, a cyclone separator, a dust remover and an induced draft fan which are sequentially connected. The circulating fluidized bed boiler system further comprises a primary air supply system and a secondary air supply system. A flue gas recirculation pipe is guided out of the rear portion of the induced draft fan and connected with the primary air supply system and the secondary air supply system in parallel. The secondary air supply system comprises a secondary air fan, a secondary air pipe, a plurality of secondary air vertical pipes arranged on the outer sides of a front wall and a rear wall of the boiler and secondary air nozzles, wherein the secondary air nozzles are arranged on a water cooling wall, connected with the secondary air vertical pipes and arranged in a dilute phase area of the boiler in a layered manner. According to the circulating fluidized bed boiler system, part of flue gas is mixed into primary air, the fluidization characteristic of a dense phase area during low-load running is improved, part of flue gas is mixed into secondary air, the air speed of the secondary air nozzles can be increased easily, a local high-temperature area is avoided, and generated NOx is reduced. By means of the secondary air arrangement manner of the system, the disturbance function of the flue gas in a hearth is increased, fuel is combusted fully, and the generated NOx is reduced.
Owner:QINGDAO JINTIAN THERMAL POWER CO LTD

Homogeneous flow-field circulating fluidized bed flue gas desulfurization technology

The invention relates to a homogeneous flow-field circulating fluidized bed flue gas desulfurization technology. A homogeneous flow-field circulating fluidized bed flue gas desulfurization reactor adopted by the homogeneous flow-field circulating fluidized bed flue gas desulfurization technology comprises a linear stream line-type flue gas inlet channel, a central built-in (center-explosion type) absorbent distributor, a flue gas accelerator, a humidifying activation nozzle, an annular flue gas outlet channel, an inner reflux circulating ash bin, a screw conveyer and an inner reflux circulating ash downcomer. The homogeneous flow-field circulating fluidized bed flue gas desulfurization technology has the advantages that a design is reasonable so that flue gas in the homogeneous flow-field circulating fluidized bed flue gas desulfurization reactor is acted upon by a homogeneous flow field, a homogeneous pressure field and a homogeneous temperature field; an absorbent has a high circulating ratio and a high utilization rate; a two-stage humidifying process can effectively improve reactivity of an absorbent; the humidifying activation nozzle is located in the center of a homogeneous flue gas flow field and a homogeneous absorbent flow field so that wall wetting, scaling and bed collapse are avoided effectively and flue gas desulfurization efficiency is improved effectively; the annular flue gas outlet channel is conducive to homogenization of a flow field in the homogeneous flow-field circulating fluidized bed flue gas desulfurization reactor and reduces a pressure drop and loads of a bag-type duster; and an inner reflux circulating conveying system can effectively prevent bed collapse and tower blocking so that safety, stability and a long running period of equipment are guaranteed.
Owner:北京博朗环境工程技术股份有限公司 +2

Flue gas desulfurization reactor of return current circulating fluidized bed in flow equalizing field

The invention relates to a flue gas desulfurization technology for a uniform flow field internal reflux circulating fluidized bed. Core equipment, namely a reactor, of the flue gas desulfurization technology comprises a direct-current streamline bottom air inlet, a guide plate, a central built-in absorbent distributor, a flue gas accelerator, a humidified activated nozzle, a rotating-stream tray gas-solid separator and a central outlet flue on the upper part of a cylinder body of the reactor form the bottom up in turn, wherein the inside of an inlet flue of the reactor is provided with a dual-chip circular uniform flue gas distribution guide plate; and the inside of the reactor is provided with the central built-in absorbent distributor, the 'Laval nozzle' - type flue gas accelerator, the two-stage double-fluid humidified activated nozzle and the rotating-stream tray gas-solid separator. The flue gas desulfurization technology is reasonable in configuration; flue gas in the reactor obtains ideal and stable uniform fluid field and temperature field; an absorbent obtains high circulation ratio and high utilization rate; and two-stage humidification can effectively improve the reaction activity of the absorbent, and can also effectively avoid wetted wall, fouling and collapsed bed. Moreover, the flue gas desulfurization technology guarantees the desulfurization efficiency, obviously reduces the dust content of the outlet flue, greatly lightens the load of a rear bag-type duster, and solves the technical problems in a flue gas desulfurization technology for a semi-dry circulating fluidized bed.
Owner:北京联合拓展科技有限公司

System and method for achieving flexible operation of circulating fluidized bed boiler based on acoustic wave technology

The invention provides a system and method for achieving flexible operation of a circulating fluidized bed boiler based on the acoustic wave technology. The system comprises the circulating fluidizedbed boiler and an acoustic wave emission device, wherein the circulating fluidized bed boiler comprises a limestone powder feeding device, a coal feeding device, a furnace, a horizontal flue, a central cylinder, a separator, a return feeder and a tail flue; and the acoustic wave emission device comprises a loudspeaker, a compression drive device and a remote control device. By means of the systemand method for achieving flexible operation of the circulating fluidized bed boiler based on the acoustic wave technology, the particle size distribution of flue gas and dust can be flexibly changed,and the circulation ratio of materials is increased through acoustic wave agglomeration effect, so that the system and the method are directly beneficial to improving the combustion efficiency of theboiler and reducing the combustible index of fly ash, and economic benefits are generated; and the system and the method are indirectly beneficial to low nitrogen combustion and reducing the emissionconcentration of SO2, NOX and other pollution gases in the boiler, so that environmental benefits are generated.
Owner:HUANENG CLEAN ENERGY RES INST

Device and method for separating CO2 by circulating fluidized bed chemical looping-combustion of coal and combustible solid waste

The invention discloses a device and a method for separating CO2 by circulating fluidized bed chemical looping-combustion of coal and combustible solid waste; the device mainly comprises three portions including a burning reaction system, a separation system and an oxygen carrying reaction system, wherein the burning reaction system is a circulating fluidized bed fuel reactor (1); the separation system comprises a one-stage inertial separator (2), a one-stage inertial separator outlet (3), a one-stage dipleg (4), a two-stage cyclone separator (11), a two-stage cyclone separator outlet (10) and a two-stage dipleg (12); the oxygen carrying reaction system comprises a cross-flow moving bed air reactor (6), a fresh oxygen carrier particle feeder (5), a J-shaped material returning valve (8) and an inactive oxygen carrier particle discharger (C); the method can enable the speed of combustion reaction of coal/combustible solid waste and oxygen carrier to be matched with the speed of oxygen carrying reaction of the oxygen carrier so as to achieve the effects that burning efficiency is high, oxygen carrying capability of the oxygen carriers is strong, concentration of separated CO2 is high, and final CO2 capturing rate is high.
Owner:SOUTHEAST UNIV

Production method and device of needle coke

PendingCN108219839ALow costSolve the long-term problems that have plagued needle coke production technologyHydrocarbon oils treatmentWaxFour-way valve
The invention provides a production method and device of needle coke. The production method comprises the following steps: clarified oil enters an evaporation section of a heat exchange condensation tower through a convection chamber of a heating furnace, oil and gas overflowing from the top of coke towers enters the evaporation section of the heat exchange condensation tower, the clarified oil exchanges heat with the oil and gas from the coke tower, components below wax oil in the clarified oil and circulating oil condensed from the oil and gas form combined oil; the combined oil enters one coke tower for coke generation through a four-way valve after being heated by a radiation chamber of the heating furnace, and the two coke towers are used for coke generation in turn; wax oil circulation is established in the heat exchange condensation tower, and part of the wax oil is pumped out. The device at least comprises a clarifying oil buffer tank, a raw material pump, the heating furnace,the coke towers, the heat exchange condensation tower, a radiation feeding pump, a wax oil pump, a wax oil evaporator and a wax oil cooler. The provided production method and device of the needle cokecan produce the high-quality needle coke, and have the advantages that process flow is simple, operability is high, industrial production is facilitated and the like.
Owner:亚通石化集团有限公司

Fused magnesium molten lump waste heat utilizing method and system

The invention relates to fused magnesium molten lump waste heat utilizing method and system. Molten fused magnesium molten lumps are sequentially sent into a magnesium molten lump waste heat recyclingchamber, a cracked magnesium molten lump waste heat recycling chamber and an automatic-deoxidizing magnesium molten lump waste heat recycling chamber so that waste heat can be recycled respectively.Turbine condensed water exchanges heat with the cracking fused magnesium molten lumps and then is sent to the automatic-deoxidizing magnesium molten lump waste heat recycling chamber to exchange heatwith the cracked fused magnesium molten lumps so that saturated water can be generated. The saturated water exchanges heat with the fused magnesium molten lumps which are just molten and then enters aflash tank so that saturated vapor can be generated and enter a turbine to be used for power generation. According to the method and the system, the fused magnesium molten lumps sequentially enter the three waste heat recycling devices so that waste heat can be recycled in stages, the finally generated saturated vapor is used for driving the turbine to generate power, the output of a system heatsource is table, the heat conversion rate is high, and the waste heat recycling efficiency is high.
Owner:ACRE COKING & REFRACTORY ENG CONSULTING CORP DALIAN MCC

Fixed bed reactor

The present invention discloses a fixed bed reactor. The fixed bed reactor comprises a shell, the shell comprises: a straight cylinder (2), a lower sealing head (1) and an upper sealing head (3), wherein the upper sealing head is provided with a reaction gas inlet (4) and a charging port (7), and the lower sealing head is provided with a manhole (11) and a discharging port (14); a lower pipe box (12) which is connected with one end, far away from the straight cylinder, of the lower sealing head and is provided with a hot water inlet connecting pipe (13); an upper tube box (6) which is connected with one end, far away from the straight cylinder, of the upper sealing head and is provided with a steam-water mixture outlet connecting tube (5); a heat exchange tube bundle (8), wherein heat exchange tubes of the heat exchange tube bundle (8) are fixed and communicated with the tube plates of the upper tube box, and the lower tube box, and the diameter of the tube plate of the upper tube box and the diameter of the tube plate of the lower tube box are smaller than the diameter of the shell; a central pipe which is used for collecting and discharging reacted gas; and a catalyst frame. According to the reactor disclosed by the invention, the heat exchange tubes can be checked and plugged without taking out internal parts, and loading and unloading of a catalyst are not hindered; and the large-angle arched heat exchange pipe is small in water circulation resistance, and reaction heat can be quickly removed.
Owner:张晓艳

Device and method for preparing sulfur by means of carbothermic reduction of SO2

The invention relates to a device and method for preparing sulfur by means of carbothermic reduction of SO2 and belongs to the technical field of sulfur recovery. The device includes a material chamber,a gas-solid mixing chamber,a carbothermic reduction tower,a high-temperature gas-solid separator,an ash hopper and a carbon-based reducing agent buffering tank. The carbothermic reduction tower includes a reaction segment and the gas-solid mixing chamber from top to bottom,the material chamber is connected to a material inlet of the gas-solid mixing chamber,a reducing gas outlet is formed in thetop of the reaction segment and connected to the high-temperature gas-solid separator,the ash hopper and the carbon-based reducing agent buffering tank in sequence,and the carbon-based reducing agentbuffering tank is connected to a material returning port of the gas-solid mixing chamber; the gas-solid mixing chamber is internally provided with a bracket,a distribution plate and a supplemented gas inlet from top to bottom in sequence. A reaction gas inlet pipe enters the gas-solid mixing chamber from the bottom of the gas-solid mixing chamber,the bracket is positioned on the lower sides of the material inlet and material returning port,one end of the reaction air inlet pipe is positioned above the bracket,and SO2 flue gas with high concentration is subjected to preliminary desulfurization; sulfur is recovered,blockage caused by accumulation of materials is avoided,and the materials are fully utilized.
Owner:SHANDONG UNIV

Method for improving circulation of materials in paper mill boiler furnace

The invention relates to a method for improving the circulation of materials in a paper mill boiler furnace. The method for improving the circulation of the materials in the paper mill boiler furnacecomprises the following steps that the temperature of the boiler furnace and the material conveying speed of feeding are detected, and the temperature of the boiler furnace and the material conveyingspeed of the feeding are kept constant; the returning air volume and the returning air pressure are detected, and the circulating ratio is calculated; if the circulating ratio is less than a preset value, the number of air cap holes of returning air and aeration air or the bore diameters of the air cap holes of the returning air and the aeration air are increased; the returning air volume and thereturning air pressure are detected in real time, and the circulating ratio is calculated again; and the steps are cycled until the circulating ratio is greater than the preset value and the returningair volume and the returning air pressure are within a preset range. Different from the prior art, according to the method for improving the circulation of the materials in the paper mill boiler furnace, by increasing the returning air volume and decreasing the returning air pressure slightly, the circulation ratio between the materials is effectively increased, the heat load rate of a boiler isevidently accelerated, and the thermal efficiency of the boiler is promoted.
Owner:LIANSHENG PAPER IND LONGHAI

System and method for gasifying and melting solid wastes

The invention discloses a system and a method for gasifying and melting solid wastes, and belongs to the technical field of environmental protection. The system comprises a solid waste feeding unit, acirculating fluidized bed gasifying unit, an entrained flow bed gasifying and melting unit, a waste heat recovery and dust removal unit and a gasified gas purification unit which are sequentially connected, the waste heat recovery and dust removal unit comprises a gasification agent preheater, a waste heat boiler, a dust remover and a gas cooler which are connected in sequence, a fly ash circulation pipeline is connected to the bottom of the dust remover, the fly ash circulation pipeline is provided with a returning unit, the circulating fluidized bed gasifying unit comprises a circulating fluidized bed gasifying furnace and a circulating fluidized bed gas-solid separator, and the returning unit is connected with the returning port of the circulating fluidized bed gas gasifying furnace. The system and the method can realize the large-scale industrial processing scale of solid wastes, and solve the problems of high energy consumption, low thermal efficiency, low gasification efficiency, poor adaptability of raw materials, incomplete harmless treatment of ash and slag, and easy entrainment of harmful substances in the smoke in existing solid waste treatment methods.
Owner:陕西德信祥能源科技有限公司
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