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42results about How to "Full use of waste heat" patented technology

Continuous pyrolysis incineration device for full-scale electronic and electrical product waste

ActiveCN105509062AGuaranteed incineration temperatureGuaranteed incineration efficiencyEmission preventionCombustion technology mitigationEnergy recoverySolvent
The invention relates to a continuous pyrolysis incineration device for full-scale electronic and electrical product waste. The continuous pyrolysis incineration device structurally comprises a feeder, a pulley feed hopper, a pyrolysis gasifier, a pyrolysis gas flue, a combustion furnace, a G-L air heat exchanger, a quenching absorption tower, a bypass flue, a chimney exhaust port, a cat ladder, an activated carbon storage tank and a chimney. The continuous pyrolysis incineration device has the advantages that dangerous electronic and electrical product waste, medical waste, organic waste and other kinds of dangerous combustible solid waste with a certain heat value are treated through a pyrolysis incineration technology, pyrolysis and high-temperature incineration technologies are combined in an optimized mode, low-temperature gas and high-temperature melt are combined together, waste incineration is conducted in the steps of pyrolysis, premixing and incineration, the synthetic technological process and technological conditions of pyrolysis incineration, energy recovery and flue gas cleaning are achieved and have perspectiveness, the overall technology has the outstanding harmless characteristic, compatibility and resourcezation are remarkable, material applicability is high, no hazardous reaction medium or poisonous and harmful solvent is involved in the process, and nature greenization can be achieved.
Owner:NANJING UNIV OF TECH

Three-tower type atmospheric-vacuum tar distillation process

The invention relates to a three-tower type atmospheric-vacuum tar distillation process. A raw material tar is dehydrated to obtain light oil fractions under constant pressure in a pre-dehydrating tower and a dehydrating tower, carrying out constant pressure operation in a No. 1 distillation tower to obtain carbolic oil and naphthalene oil fractions, and carrying out reduced pressure operation in a No. 2 distillation tower to obtain washing oil, primary anthracene oil, secondary anthracene oil and medium-temperature asphalt under or obtain the washing oil, the primary anthracene oil and maltha products. Heats of the pre-dehydrating tower and the dehydrating tower are provided by heat-conduction oil or steam; the heat of the No. 1 distillation tower is circularly provided by tower bottom mixing oil in a No. 1 tube-type heating furnace; and the heat of the No. 2 distillation tower is circularly provided by tower bottom asphalt in a No. 2 tube-type heating furnace. A main device comprises the dehydrating tower, the No. 1 distillation tower, the No. 2 distillation tower, a dehydrating tower reboiler, the No. 1 tube-type heating furnace, the No. 2 tube-type heating furnace, each fraction heat exchanger, a cooler, a pump and the like. The three-tower type atmospheric-vacuum tar distillation process disclosed by the invention has the advantages of being simple and quick in process flow, simple and convenient in operation, low in capital construction investment, energy-saving and environment-friendly, and is suitable for coal tar processing engineering capable of annularly processing anhydrous tar in the scale of more than 2,000,000 tons.
Owner:ACRE COKING & REFRACTORY ENG CONSULTING CORP DALIAN MCC +1

Steam generator for kitchen

The invention relates to a cooking utensil, in particular to a steam generator for a kitchen. The steam generator for the kitchen comprises a shell and is characterized in that the shell is provided with a steam generation cavity, a smoke collecting cavity and a smoke exhausting cavity sequentially from bottom to top; a tube plate is arranged between the steam generation cavity and the smoke collecting cavity; a gas stove installing cavity is arranged outside a bottom plate; the steam generation cavity comprises a plurality of smoke tubes installed in the vertical direction; the lower ends of the smoke tubes penetrate through the bottom plate and extend to the outside of the shell, and the upper ends of the smoke tubes penetrate through the tube plate to extend to the smoke collecting cavity; a steam output pipe is arranged on the steam generation cavity; and a smoke exhausting outlet is formed in the top of the smoke exhausting cavity. The smoke exhausting cavity is further provided with a heat exchange tube set, the two ends of the heat exchange tube set are provided with a water injection port and a water outlet correspondingly, and the water outlet is supplemented to the steam generation cavity through a pipeline. The steam generator for the kitchen has the beneficial effects that the steam generation efficiency is high, the structure is simple, maintenance is convenient, and the steam generator can be conveniently connected with other steaming utensils through pipelines and is clean and hygienic.
Owner:YANTAI ZHONGDE ENVIRONMENTAL PROTECTION EQUIPTECH

Device for recycling hot waste gas generated in production process of -2-aminobutyric acid salt ammonium salt and using method thereof

The invention disclose a device for recycling hot waste gas generated in the production process of -2- aminobutyric salt ammonium salt and a using method thereof. The device comprises a drying chamber, a hot waste gas pipe, a brick baking chamber, an exhaust pipe, a purification tower, gas inlets, a conveyor belt, rotating shafts, a first gas inlet pipe, a second gas inlet pipe, a spiral pipe, a water tank, a water pumping port and a partition plate. The device has the beneficial effects that the drying chamber and the brick baking chamber are connected together through the hot waste gas pipeso that the hot waste gas generated through baking the bricks can be recycled to dry green bricks; the gas inlets of the hot waste gas pipe are formed in the two sides of the drying chamber, the convection of the hot waste gas can be realized through the two gas inlets, the hot waste gas can be uniformly mixed, so that the contact area between the green bricks and the hot waste gas is increased, and the drying speed is accelerated; and the water tank is arrange on the partition plate, the circle of spiral pipe is arranged on the outer wall of the periphery of the water tank, and therefore theused hot waste gas passes through the spiral pipe to heat the water tank, and the waste heat of the hot waste gas is fully utilized. The device has the characteristics of being high in drying speed and capable of better utilizing the waste heat.
Owner:浙江双鸿新能源科技有限公司

Box type evaporator for waste heat utilization of high-temperature solid materials

The invention discloses a box type evaporator for waste heat utilization of high-temperature solid materials and belongs to the field of cooling equipment for the high-temperature solid materials. The box type evaporator is characterized in that an outer cylinderl (2) and an inner cylinder (1) are combined to form a sleeve type header; the lower end of a heat exchange box (7) is open; the sleeve type header seals the upper end of the heat exchange box (7); a feeding port (4) communicated with the inner cylinder (1) is arranged at the upper part of the sleeve type header; a water-cooled spiral distributor for conveying and cooling the materials is arranged inside the inner cylinder (1); a heat exchange cavity is arranged on the side wall of the heat exchange box (7) ad is communicated with an inner cavity of the outer cylinder (2); multiple isolating mechanisms are arranged inside the heat exchange box (7) in parallel and divide the heat exchange box (7) into multiple material channels; and the materials in the inner cylinder (1) fall into the material channels via discharge ports (6). Both the sleeve type header and the heat exchange box of the box type evaporator for waste heat utilization of the high-temperature solid materials can bear pressure, so that the evaporator can be directly applied to production of steam, and waste heat of the high-temperature materials is efficiently utilized.
Owner:SHANDONG LIANXING ENERGY SAVING SERVICE

System used for coal-fired power plant waste-heat utilization and desulfuration water saving

The invention discloses a system used for coal-fired power plant waste-heat utilization and desulfuration water saving. The system comprises a steam turbine, a first-level heat exchanger, a second-level heat exchanger, a condensate pump and an air pre-heater. The air inlet end of the steam turbine is connected with a boiler, and the exhaust air output end of the steam turbine is connected with the air inlet end of a condenser. The first-level heat exchanger is arranged in an absorption tower slurry pond at the bottom of a desulfuration absorption tower. The second-level heat exchanger is arranged between the desulfuration absorption tower and a dust remover, and the liquid inlet end of the second-level heat exchanger is connected with the liquid outlet end of the first-level heat exchanger. The liquid outlet end of the second-level heat exchanger is connected with an inlet pipeline of a fifth-level low-pressure heater. The air outlet end of the dust remover is connected with the air inlet end of the second-level heat exchanger. An outlet pipeline of the fifth-level low-pressure heater is connected with the boiler. The liquid inlet end of the condensate pump is connected with the liquid outlet end of the condenser, and the liquid outlet end of the condensate pump is connected with the first-level heat exchanger. The air inlet end of the air pre-heater is connected with the boiler, and the air outlet end of the air pre-heater is connected with the air inlet end of the dust remover.
Owner:DATANG ENVIRONMENT IND GRP

Full-scale electronic and electrical waste continuous pyrolysis incineration device

ActiveCN105509062BInhibitionTo achieve the purpose of volume reductionEmission preventionCombustion technology mitigationEnergy recoverySolvent
The invention relates to a continuous pyrolysis incineration device for full-scale electronic and electrical product waste. The continuous pyrolysis incineration device structurally comprises a feeder, a pulley feed hopper, a pyrolysis gasifier, a pyrolysis gas flue, a combustion furnace, a G-L air heat exchanger, a quenching absorption tower, a bypass flue, a chimney exhaust port, a cat ladder, an activated carbon storage tank and a chimney. The continuous pyrolysis incineration device has the advantages that dangerous electronic and electrical product waste, medical waste, organic waste and other kinds of dangerous combustible solid waste with a certain heat value are treated through a pyrolysis incineration technology, pyrolysis and high-temperature incineration technologies are combined in an optimized mode, low-temperature gas and high-temperature melt are combined together, waste incineration is conducted in the steps of pyrolysis, premixing and incineration, the synthetic technological process and technological conditions of pyrolysis incineration, energy recovery and flue gas cleaning are achieved and have perspectiveness, the overall technology has the outstanding harmless characteristic, compatibility and resourcezation are remarkable, material applicability is high, no hazardous reaction medium or poisonous and harmful solvent is involved in the process, and nature greenization can be achieved.
Owner:NANJING TECH UNIV

Two-tower type pressure reducing coke tar distillation process and apparatus therefor

ActiveCN101475819BSolve the technical problems of dealing with large-scale tarShort processTar working-up by distillationHeat conductingReboiler
The invention relates to a two-tower type process for distilling vacuum tar and a device thereof. The process comprises the following steps: removing the moisture and light oil distillate of raw tar in a pre-dehydration tower and a dehydration tower at normal pressure; performing decompressing operations in a No.1 distillation tower to obtain carbolic oil, naphthalene oil and light washing oil distillate; and performing decompressing operations in a No.2 distillation tower to obtain heavy washing oil, first anthracene oil, second anthracene oil and mid-temperature pitch. The heat for the pre-dehydration tower and the dehydration tower is supplied by heat conducting oil; the heat for the No.1 distillation tower is supplied by heating the mixed oil on the bottom of the tower circularly in aNo.1 tubular heating furnace; and the heat for the No.2 distillation tower is supplied by heating the mixed oil on the bottom of the No.1 distillation tower in a No.2 tubular heating furnace and thenperforming flash distillation on the mixed oil on the bottom of the No.2 tower. The main devices comprise the dehydration tower, the No.1 distillation tower, the No.2 distillation tower, a dehydration tower reboiler, the No.1 tubular heating furnace, the No.2 tubular heating furnace, a heat exchanger for each distillate, a cooler, a steam generator and the like. The process has the advantages of short technological flow, less device investment, and less energy consumption, thus the process is applicable to large scale coal tar processing engineering.
Owner:ACRE COKING & REFRACTORY ENG CONSULTING CORP DALIAN MCC

Process and apparatus for dry suspension sintering flash smelting of ferronickel

PendingCN108239708AReduce energy costsImprove production efficiency and social benefitsProcess efficiency improvementFlue gasPower consumption
The invention relates to a process and apparatus for dry suspension sintering flash smelting of ferronickel, belonging to the field of ferronickel production processes and apparatuses. The process comprises the following steps: 1) drying; 2) grinding; 3) multi-stage suspension pre-reduction; 4) sintering reduction; and 5) flash furnace smelting. Flue gas with waste heat from flash furnace successively enters a sintering furnace and a multi-stage suspension pre-reduction system; the heat and a reducing agent in the flue gas act on the links of pre-reduction and sintering reduction, so the wasteheat is utilized, and energy consumption is reduced; and mineral materials in the flue gas settle down in a preheating system and then return to a melting system, so productivity is enhanced and theemissions of pollutants are lowered. Material flow in the whole system operates in a closed loop, and exhaust gas is purified and then discharged after reaching the standard. The apparatus comprises adrying device, a grinding device and a dry suspension sintering device, wherein the drying device, the grinding device and the dry suspension sintering device are sequentially connected. The processand apparatus of the invention has the advantages of low investment cost, obvious energy saving effect, no consumption of electricity and coke, greatly-reduced power consumption, substantially-loweredcost for reducing agents, full utilization of exhaust gas and waste heat and high automation degree.
Owner:徐州贝克福尔节能环保技术有限公司

Boiler waste heat utilization water heater

The invention relates to the field of waste heat utilization, in particular to a boiler waste heat utilization water heater. The boiler waste heat utilization water heater comprises a hopper, a smokeinlet, a water feeding mechanism, first water valves, water pipes, a water box, supporting frames, a box body, a water drainage mechanism, water drainage pipes, second water valves, temperature gauges, a supporting mechanism, supporting rods, a supporting plate, heating mechanisms, first water heating boxes, second water heating boxes, a blocking mechanism, a first fixing plate, a baffle, a secondfixing plate, a smoke outlet and a sealing mechanism. According to the boiler waste heat utilization water heater, the side walls of the two ends of the box body are provided with the smoke inlet andthe smoke outlet correspondingly, the heating mechanisms distributed in a staggered mode are installed in the box body, waste gas enters the box body to make sufficient contact with the heating mechanisms, and thus, heat in the waste gas enters the heating mechanisms; and the side wall of the box body is rotationally connected with the sealing mechanism, the sealing mechanism is rotated so that the interior of the box body can be opened, the hopper is installed at the bottom end of the box body, dust inside the box body is removed through a shovel, and accordingly, dust in the box body and dust on the side walls of the heating mechanisms are discharged from the hopper.
Owner:安徽原上草节能环保科技有限公司

Biomass steam generator

The invention discloses a biomass steam generator, and relates to the field of boilers. The biomass steam generator comprises a rack, a furnace body of a biomass combustion chamber arranged in the rack, a boiler body heated on the furnace body and a steam chamber, wherein the steam chamber is positioned at the top end of the boiler body and communicates with the boiler body; a feeding port and a smoke discharging pipe further communicate with the furnace body and are arranged on the furnace body; a dust removing and filtering device is arranged on the side wall of the rack, and the dust removing and filtering device comprises a filtering box fixedly connected to the rack and a water spraying assembly arranged in the filtering box; the water spraying assembly communicates with a water source through a water inlet pipe; the smoke discharging pipe communicates with the position, close to the bottom, of the filtering box; a water storage box is arranged below the filtering box; the bottomof the filtering box is connected with a water discharging pipe for discharging water to the water storage box; and an air outlet pipe is arranged at the top of the filtering box. Through the arrangement of the dust removing and filtering device, the situation that dust enters the outside air is reduced through the water spraying assembly, so that the influence of the dust in the smoke on the environment is reduced.
Owner:ZHEJIANG RUYI IND

Waste heat collecting cover of cooking range

The invention discloses a waste heat collecting cover of a cooking range. The waste heat collecting cover comprises a collecting cover body, an isolation layer and a heat exchange water pipe; the top and the bottom of the collecting cover body are each provided with an opening, and the opening in the top of the collecting cover body is sealed through a heating body; the opening in the bottom of the collecting cover body, and the collecting cover body is placed on the cooking range; the isolation layer is arranged in the collecting cover body to separate space in the collection cover body into a heating area and a waste heat collecting area, and a fire spraying opening of the cooking range is placed in the heating area; the top of the heating area and the top of the waste heat collecting area are communicated, and waste heat for the heating area enters the waste heat collecting area from the top of the heating area; the heat exchange water pipe is arranged in the waste heat collecting area; and the heat exchange water pipe is arranged around the isolation layer, one end of the heat exchange water pipe stretches out of the collecting cover body to be communicated with a water source, and a discharging opening controlled by a valve is formed in the position, arranged on the collecting cover body, of the other end of the heat exchange water pipe.
Owner:马志强

By-product steam hydrogen chloride graphite synthesis furnace with economizer

The invention is mainly applied in the technical field of hydrogen chloride synthesis, and in particular relates to a byproduct steam hydrogen chloride graphite synthetic furnace provided with a coal economizer. The byproduct steam hydrogen chloride graphite synthetic furnace provided with the coal economizer comprises a graphite furnace cylinder and a steam pocket, wherein a gas remixer is arranged in the top of the graphite furnace cylinder; an evaporation structure section, a coal economizer section and a cooling structure section which are hermetically connected are arranged at the top of the gas remixer sequentially from bottom to top; the upper part and the lower part of an evaporation section metal structure cylinder body are connected in series with the steam pocket through circulating pipelines; an integrated furnace bottom seal head is arranged at the bottom of the graphite furnace cylinder; a premixing type synthetic furnace lamp holder is arranged on the integrated furnace bottom seal head; an integrated furnace top seal head is arranged at the top of the cooling structure section; and a hydrogen chloride outlet is formed in the integrated furnace top seal head. According to the byproduct steam hydrogen chloride graphite synthetic furnace with the coal economizer, heat energy carried by the hydrogen chloride can be recovered to be used for preheating deionized water of the byproduct steam, the waste heat is utilized more completely and the heat utilization rate is increased; meanwhile, the hydrogen chloride is further cooled, the cooling load is reduced, and the advantages of energy conservation, consumption reduction, complete utilization of the waste heat and high heat utilization rate.
Owner:山东赫达集团股份有限公司
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