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81results about How to "Increase waste heat recovery" patented technology

Blast furnace smelting slag water quenching waste steam waste heat recovery system

The present invention provides a blast furnace smelting slag water quenching waste steam waste heat recovery system. The system comprises a blast furnace slag water quenching apparatus, a slag quenching water circulation apparatus and a waste steam waste heat recovery apparatus. The blast furnace slag water quenching apparatus comprises a smelting slag groove, a water quenching apparatus and a slag discharging and conveying belt. The slag quenching water circulation apparatus comprises the water quenching apparatus, a water circulating tank, a water quenching pump and a water supplying pipe. The waste steam waste heat recovery apparatus comprises the water quenching apparatus, a three-phase separator, a fan, a heat exchanger, a hot water pump and a low-temperature user. The method of the present invention is different from the method in the prior art, wherein the recovery of the slag quenching waste water waste heat is adopted to recover the smelting slag waste heat by the method in the prior art, and the waste heat in the waste steam generated from the smelting slag quenching by the recovered water is adopted to recover the smelting slag waste heat by the method of the present invention, the water quality of the waste steam is better than the water quality of the waste water, such that the disadvantages of high hardness of the waste water, equipment scaling, equipment blocking and the like in the prior art are overcome. According to the present invention, the slag quenching waste steam waste heat is effectively recovered; the system has advantages of energy saving and emission reduction, and environmental protection; the collected waste heat can be used to meet the requirements of the low-temperature user.
Owner:ANHUI UNIVERSITY OF TECHNOLOGY

Evaporator capable of utilizing waste heat

The invention discloses an evaporator capable of utilizing waste heat. The evaporator comprises a soot gas inlet pipe, a dust removing square pipe and an evaporator body; the soot gas inlet pipe is inflange connection to the inlet end of the dust removing square pipe, the evaporator body comprises a casing and further comprises a hot fluid inlet pipe, a hot fluid outlet pipe, a cold fluid inlet pipe, a cold fluid outlet pipe and a spiral heat exchange pipe which are fixedly welded to the casing, the hot fluid inlet pipe is in flange connection to the outlet end of the dust removing square pipe, a filter mesh frame is fixedly welded to the inner pipe wall of the dust removing square pipe, the inner wall of the filter mesh frame is fixedly connected with a filter net, a comb brush for cleaning the filter net is arranged on the side, close to the soot gas inlet pipe, of the filter net, and the comb brush moves vertically in the dust removing square pipe along with a sliding sleeve. According to the evaporator, hot soot gas is used for exchanging heat with cold water in the evaporator, and therefore hot steam can be used for production and life; and soot particles are filtered out through the filter net to avoid blockage of the evaporator, the heat utilization rate is high, the structure is simple, operation is easy, and energy saving and environmental protection are achieved.
Owner:江苏世林博尔制冷设备有限公司

Flue gas waste heat recovery unit

The invention relates to a flue gas waste heat recovery unit which comprises a flue gas unit, a generator unit, a condenser unit, an absorber unit, a water return pipe and a water supply pipe. The flue gas unit is sequentially connected with the generator unit, the condenser unit and the absorber unit to form a flue gas heat exchanging path; the outlet of the generator unit is connected with the inlet of a solution-to-solution heat exchanger, the outlet of the absorber unit is divided into two paths: one path is merged with the outlet of the solution-to-solution heat exchanger to be connected with the inlet of a solution-to-water heat exchanger through a solution spray pump, the outlet of the solution-to-water heat exchanger is connected with a solution spray mechanism in the absorber unit, the other path is connected with the inlet of a solution-to-solution heat exchanger through a solution circulating pump, and the outlet of the solution-to-solution heat exchanger is connected with a dilute solution spray mechanism through the generator unit so as to form a solution heat exchanging and circulating loop; the outlet of the condenser unit is connected with the inlet of a water-to-water heat exchanger through a condense water spray pump, the outlet of the water-to-water heat exchanger is connected with a condense water spray mechanism through the condenser unit to form a condense water heat exchanging and circulating loop; the water return pipe is connected with a water-to-water heat exchanger unit and the inlet of a solution-to-water heat exchanger, and the water supply pipe is connected with the water-to-water heat exchanger and the inlet of the solution-to-water heat exchanger.
Owner:TSINGHUA UNIV +1

Low-vacuum absorption-type composite heat pump residual heat supply system based on ultra-great-temperature-difference heat supply network

The invention relates to a low-vacuum absorption-type composite heat pump residual heat supply system based on an ultra-great-temperature-difference heat supply network, and belongs to the field of residual-heat-recovery-type cogeneration based on low-vacuum circulation water heating as well as absorption-type heat exchange. The low-vacuum absorption-type composite heat pump residual heat supply system comprises an absorption-type heat pump residual heat recovery device, a peak adjusting heater, a heat supply network ultra-great-temperature-difference heat exchange machine set as well as pipeline components. The low-vacuum absorption-type composite heat pump residual heat supply system is characterized by also comprising a direct dead steam recovery device as a water-based heat loading source of the heat supply network; a cold side inlet of the device is connected with a water return pipe of the heat supply network, and an outlet of the device is connected with a water inlet of an absorption-type heat pump heat supply network; a water outlet of the absorption-type heat pump heat supply network is connected with a water of a heat supply network of the peak adjusting heater; a water outlet of the heat supply network of the peak adjusting heater is connected with a water supply pipe of the heat supply network; dead steam enters the direct dead steam recovery device and the absorption-type heat pump evaporator. The low-vacuum absorption-type composite heat pump residual heat supply system provided by the invention is relatively higher in efficiency for thermal power plants than that in the conventional recovery mode for extracting residual heat from cooling water, can improve the dead steam residual heat utilization quantity by more than 1-2 times, and is especially suitable for central heat supply systems of middle and large sized turbosets.
Owner:张茂勇

Novel solar drying system

The invention discloses a novel solar drying system. The novel solar drying system comprises a solar air heat gatherer, an air blower, a solar battery, a drying box, a temperature and humidity controller, a valve and a heat exchanger. The novel solar drying system is characterized in that the heat exchanger is provided with a first air inlet, a second air inlet, a first air outlet and a second air outlet; an insert pipe is arranged in each vacuum heat gathering pipe of the solar air heat gatherer, and the insert pipes are connected with an air buffer backflow zone header after passing through the top of a hot air flow passage zone header; the air blower is arranged between the air outlet of the heat gatherer and the air inlet of the drying box; an air flow passage zone is arranged in the side of the inside of the drying box near the air blower, and a material drying zone is arranged at the other side; an induction probe of the temperature and humidity controller is arranged at the air outlet of the drying box; an air return pipeline led from the air outlet of the drying box is divided into two branches, one branch is connected with the first air inlet of the heat exchanger through a second valve, the other branch is further divided into two passages after passing through the first valve, one passage is directly connected with the air inlet of the heat gatherer header, and the other passage is connected with the first air outlet of the heat exchanger through a third valve.
Owner:YUNNAN NORMAL UNIV

Low vacuum ejector heat pump composite waste-heat heating supply system based on huge temperature-difference heat supply network

The invention relates to a low vacuum ejector heat pump composite waste-heat heating supply system based on a huge temperature-difference heat supply network, and belongs to the field of waste-heat recovery type combined heat and power generation based on low vacuum circulation water heating and heat exchange of an ejector heat pump. The system is characterized by comprising an ejector heat pump waste-heat recovery device, a dead-steam direct recovery device, a pitch peak heater, a heat supply network huge temperature-difference heat exchange unit and a pipe fitting, wherein the dead steam is taken as a water-based load heat source of the heat supply network; a cold-side inlet of the dead steam direct recovery device is connected with a water return pipe of the heat supply network; an outlet is connected with a heat supply network water inlet of an ejector heat pump condenser; then the dead steam is sent to the pitch peak heater to be heated to the required temperature, and then exhausted out; at last, the dead steam is sent into the dead-steam direct recovery device, and an ejection port in the ejection section of the ejector heat pump. The system can be used for a thermal power plant with higher efficiency than the conventional recovery way that waste-heat is extracted from cooling water, the utilization amount of the dead-steam waste heat can be improved by more than 1-2 times, while the investment is only a part of that of an absorption heat pump.
Owner:张茂勇

Semi-open high-temperature heat pump system and working method thereof

The invention provides a semi-open high-temperature heat pump system. The system comprises a compressor, a contact condenser, a heat exchanger, an evaporator, a water purifier, a cold water pump, a hot water pump, a circulating water pump and a vacuum pump. An exhaust port of the compressor is connected with the contact condenser, the contact condenser is connected with the evaporator through theheat exchanger, the evaporator is connected with the compressor air suction port through an upper exhaust port, an outlet of the water purifier is correspondingly connected with the compressor, the contact condenser and the evaporator through the cold water pump, a lower outlet of the evaporator is connected with the contact condenser through the circulating water pump, the upper part of the contact condenser is connected with the vacuum pump, and the lower part of the contact condenser is connected with the hot water pump. According to the system, water is adopted as a circulating working medium, and the contact condenser with high heat transfer efficiency is adopted, so that the system has the characteristics of being environment-friendly and high in efficiency, can recover low-temperature waste heat of 50 DEG C or above, and provides high-temperature hot water of 90 DEG C or above. Compared with the prior art, the system effectively reduces the heat transfer thermal resistance, improves the heat transfer efficiency, effectively recovers the low-temperature waste heat, improves the heat source quality, and achieves reuse.
Owner:JIANGSU UNIV OF SCI & TECH

Coke oven hydrogen utilization method and system

The invention relates to the field of coke furnaces, particularly to a coke oven hydrogen utilization method and system. The method is especially suitable for hydrogen-rich comprehensive utilization of raw coke oven gas in different coke curing periods of a coke oven coking process. The method comprises the following steps: sequentially introducing hydrogen-rich raw coke oven gas obtained in a later period of coking from one or more carbonization chambers into another carbonization chamber or a plurality of other carbonization chambers which are just filled with coal through a raw coke oven gas pipe duct system; allowing the introduced hydrogen-rich raw gas to form a hydrogen-rich environment in the carbonization chambers which are just filled with the coal; and enabling a cracking reaction to realize conversion to a light target product by controlling, adjusting and inducing the cracking reaction of the raw gas. The furnace tops of the carbonization chambers have high-temperature hydrogen which has very high activation energy and can undergo a hydrogenation reaction with graphite at the top of the carbonization chambers for secondary cracking of coal tar, so the charring procedureof opening a furnace cover 10-20 minutes ahead of time in the processes of combustion and decoking is eliminated, tar yield is increased, and coke oven productivity is improved.
Owner:葛霖

Cooling, heating, water supplying and power supplying combined system with flue gas heat gradient utilization function coupled with seawater desalination technology

The invention discloses a cooling, heating, water supplying and power supplying combined system with a flue gas heat gradient utilization function coupled with a seawater desalination technology. The cooling, heating, water supplying and power supplying combined system comprises a gas turbine generator set, a hybrid heat source double-effect lithium bromide system, a seawater desalination evaporator, a primary preheater, a secondary preheater and a low-level water tank; an exhaust outlet of a gas turbine is connected with a flue gas inlet of the seawater desalination evaporator; a flue gas outlet of the evaporator penetrates through a high pressure generator of a lithium bromide unit via a pipeline and is connected with a flue gas outlet of the lithium bromide unit, a steam outlet of the evaporator is divided into two pipelines, one pipeline of the steam outlet of the evaporator penetrates through a low pressure generator of the lithium bromide unit, and the other pipeline of the steam outlet of the evaporator penetrates through a first heat exchanger of the hybrid heat source double-effect lithium bromide system to be communicated with the low-level water tank; and a condensate outlet of the lithium bromide unit is connected with the low-level water tank, and the flue gas outlet of the lithium bromide unit penetrates through the secondary preheater via a pipeline and then exhausts flue gas to an environment. The cooling, heating, water supplying and power supplying combined system has the advantages that a flue gas waste heat utilization rate and an energy utilization rate of devices are high, the cooling, heating, water supplying and power supplying combined system is applicable to running under different working conditions, a cooling load, a heating load and a power load can be matched with one another easily, and the like.
Owner:JIMEI UNIV

Temperature distributing cooling method and temperature distributing unloading device for sintered ores

ActiveCN106323013AAchieve separationSolve the problem of traditional cooling processCharge manipulationHandling discharged materialMetallurgyHot Temperature
The invention discloses a temperature distributing cooling method for sintered ores. The method comprises the following steps of: determining a sintered ore layer, the temperature of which is lower than the unloading temperature of a ring cooling machine, as a low-temperature sintered ore layer and determining a sintered ore layer, the temperature of which is higher than the unloading temperature of the ring cooling machine, as a high-temperature sintered ore layer according to the temperature distribution of the sintered ore layer in a trolley of a sintering machine in the tail part of the sintering machine; performing temperature distributing unloading on the tail part of the sintering machine so as to separate the low-temperature sintered ore layer and the high-temperature sintered ore layer, wherein the low-temperature sintered ore layer which is crushed does not enter the ring cooling machine but is directly conveyed to a follow-up screening step, and the high-temperature sintered ore layer which is crushed enters the ring cooling machine for a cooling operation. The process method can remarkably reduce the handling capacity of the sintered ores in the ring cooling machine by improving the unloading mode of the sintered ores and the material distributing mode on the ring cooling machine, so that the cost of the ring cooling machine is lowered, and the waste heat recovery amount of the sintered ores is improved. The invention further discloses a temperature distributing unloading device used by the method.
Owner:ZHONGYE-CHANGTIAN INT ENG CO LTD

Sinter distributed temperature cooling method, sinter time-sharing unloading trolley and distributed temperature unloading device

The invention discloses a sinter distributed temperature cooling method. The method comprises the following steps: determining sinter layers with temperatures lower than the unloading temperature of a circular cooler as low temperature sinter layers and determining other sinter layers as high temperature sinter layers according to temperature distribution of sinter layers in a sintering machine trolley at the tail of a sintering machine; and carrying out time-sharing unloading during unloading at the tail of the sintering machine to achieve separation of the low temperature sinter layers and the high temperature sinter layers, wherein the low temperature sinter layers do not enter the circular cooler but are directly conveyed to a follow-up screening procedure after being crushed, and the high temperature sinter layers enter the circular cooler to undergo cooling operation after being crushed. The method has the beneficial effects that the handling capacity of the sinter in the circular cooler can be obviously reduced, the cost of the circular cooler can be reduced and the sinter waste heat recovery can be increased by improving the sinter unloading method and the method of sinter distribution on the circular cooler. The invention also discloses a sinter time-sharing unloading trolley and a distributed temperature unloading device.
Owner:ZHONGYE-CHANGTIAN INT ENG CO LTD

Intelligently-controlled open type compression absorption heat pump system for water and waste heat recovery

ActiveCN113686052AGuaranteed solution flowAdjust absorbencyHeat pumpsHeat recovery systemsData connectionAbsorption heat pump
The invention provides an intelligently-controlled open type compression absorption heat pump system for water and waste heat recovery. An outlet of a gas pipeline is connected with a contact heat exchanger, a circulating solution pump I is arranged on a pipeline between an absorber and a solution heat exchanger, and a circulating solution pump II is arranged on a pipeline between a regenerator and the solution heat exchanger; and a temperature and humidity and/or pressure sensor is arranged at a gas outlet at the upper portion of the contact heat exchanger and used for detecting the temperature and humidity and/or pressure of exhausted gas, and the circulating solution pump I, the circulating solution pump II and the temperature and humidity and/or pressure sensor are in data connection with a controller. The controller automatically adjusts the compression power of the circulating solution pump I and the circulating solution pump II according to the detected temperature and humidity and/or pressure, so that the flow of absorption solutions entering the absorber and the regenerator is adjusted to meet the requirements of water vapor absorption and solution regeneration in gas, and the moisture content parameter of the gas outlet is further changed. The power of the circulating solution pump I and the power of the circulating solution pump II are controlled through the temperature and pressure of outlet gas of the contact heat exchanger, the flow of the solutions entering the absorber and the regenerator can be guaranteed, and then the absorption and regeneration effects are adjusted; and finally, the temperature and pressure parameters of the gas in the contact heat exchanger and the absorber are kept in a relative balance state, and the system has extremely high engineering practical significance.
Owner:SHANDONG UNIV

Compound type two-stage lithium bromide absorption type heat pump and working method

The invention discloses a compound type two-stage lithium bromide absorption type heat pump and a working method. The lithium bromide absorption type heat pump comprises two lithium bromide heat pumpunits which are mutually connected; the first lithium bromide heat pump unit comprises a first evaporator, a first generator, a first absorber and a first condenser which are mutually connected; the second lithium bromide heat pump unit comprises a second evaporator, a second generator, a second absorber and a second condenser which are mutually connected; and the output end of a heat exchange pipe of the first absorber sequentially communicates with heat exchange pipes of the second absorber, the second condenser and the first condenser. The invention further discloses the working method of the compound type two-stage lithium bromide absorption type heat pump. On the one hand, under the conditions that medium warm water and low warm water conditions are certain, the temperature of the unit generators is reduced, and the service life of the units is prolonged; on the other hand, the steam discharge range of the units is enlarged, the type selection of the units is reduced advantageously, and the cost is reduced; and the units are very convenient to manufacture.
Owner:BROAD AIR CONDITIONING CO LTD

Open type compression absorption heat pump system for water heat recovery in high-temperature and high-humidity gas

The invention provides an open type compression absorption heat pump system for water heat recovery in high-temperature and high-humidity gas. An outlet of a gas pipeline is connected with a contact heat exchanger, a gas pressure adjusting device is arranged on the gas pipeline, the contact heat exchanger is connected with an absorber, a gas outlet at the upper end of the absorber is connected with an expansion machine, and a first pressure control valve is arranged on a pipeline between the absorber and the expansion machine; a circulating water inlet is connected with a solution water heat exchanger, the solution water heat exchanger is connected with a condenser, the condenser is connected with the contact heat exchanger, the lower end of the contact heat exchanger is connected with a circulating water tank, the circulating water tank is connected with a user side heat output device, and the user side heat output device is connected with the solution water heat exchanger; the absorber is connected with a solution heat exchanger, the solution heat exchanger is connected with a regenerator, the regenerator is connected with the solution heat exchanger, the solution heat exchanger is connected with the solution water heat exchanger, and the solution water heat exchanger is connected with the absorber; the regenerator is connected with the condenser, and the condenser is connected with a vacuum pump; and the expansion machine conveys energy to the vacuum pump. According to the system, utilization of waste heat of high-temperature and high-humidity gas, recovery of water, capturing of pollutant components and reuse of gas expansion work can be further realized, and the system has extremely strong engineering practical significance.
Owner:SHANDONG UNIV

Membrane type fixed bed catalyst raw coke oven gas waste heat recovery and hydrogen utilization ascending pipe

The invention discloses a membrane type fixed bed catalyst crude gas waste heat recovery and hydrogen utilization ascending pipe. The pipe comprises an ascending pipe shell and a bridge pipe tee joint; a raw gas channel is formed in the ascending pipe, and the ascending pipe further comprises a cylinder wall heat preservation layer, a temperature control and waste heat recovery device, an anti-corrosion ceramic layer and a membrane type fixed bed catalyst layer; the inner layer of the pipe wall of the shell of the ascending pipe is a barrel wall heat preservation layer, a temperature control and waste heat recovery device is arranged on the inner ring of the barrel wall heat preservation layer, and a working medium for taking away waste heat of raw coke oven gas is introduced into the temperature control and waste heat recovery device; an anti-corrosion ceramic layer is attached to the surface of the outer layer of the temperature control and waste heat recovery device, or a mixed layer formed by combining the anti-corrosion ceramic layer and a membrane type fixed bed catalyst layer is attached to the surface of the outer layer. According to the invention, the hydrogen-rich raw coke oven gas is subjected to directional reaction at a proper temperature under the action of the catalyst, the technical bottleneck problem in the existing coke oven production process is eliminated, the reliability and stability of the riser are improved, and the long-term stable and safe operation of the system is facilitated.
Owner:扬州优为节能科技有限公司

Movable tank type cooler and sinter cooling method

ActiveCN107796227AUniform flow fieldStructural factors to eliminate air leakageHandling discharged materialWaste heat treatmentFlueWaste heat
The invention discloses a movable tank type cooler. The cooler comprises 1) a ring-groove-shaped cooling bin, 2) a drive device driving the ring-groove-shaped cooling bin to move, 3) an annular hot air cover arranged on the ring-groove-shaped cooling bin, 4) at least one hot air collecting pipe connected to the top or the side portion of the hot air cover, 5) a cooling air flue arranged on the inner side of the ring-groove-shaped cooling bin, 6) an annular rotation rack arranged at the bottoms of the ring-groove-shaped cooling bin and the cooling air flue, 7) an ore discharging bucket arrangedat the lower portion of the ring-groove-shaped cooling bin, 8) a plurality of cooling draught fans and 9) a cooling air communication pipe. The cooling air flue comprises a cooling air flue moving base and a cooling air flue fixing cover. An air passing beam is arranged in the annular rotation rack in a hollow manner. Air outlets of the cooling draught fans communicate with the cooling air flue through cooling air pipes corresponding to the cooling draught fans. The cooling air communication pipe is arranged between the cooling air flue moving base and the annular rotation rack. According tothe movable tank type cooler, all air leakage links are eliminated, good sealing performance of movable tank cooling is guaranteed, and the waste heat recycling amount is greatly increased.
Owner:ZHONGYE-CHANGTIAN INT ENG CO LTD
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