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57results about How to "Good temperature matching" patented technology

Heat and humidity segmented treatment air-conditioning device and method combined with radiation cold supply

The invention discloses a heat and humidity segmented treatment air-conditioning device and method combined with radiation cold supply. The device mainly comprises a cold water unit, an air treater, a radiation coil pipe, a water pump, an electromagnetic valve and a pipeline. In a system, chilled water obtained by the cold water unit is used for cooling and dehumidifying air, and is supplied to a ceiling or a floor radiation coil pipe for radiation cold supply to realize segmented treatment of heat and humidity loads in a room. The radiation coil pipe is used for supplying cold and bearing a part of sensible heat load in the room, and dehumidified supply air is used for bearing the other part of sensible heat load in the room and indoor humidity load and preventing a radiation surface from moisture condensation. Chilled water is segmentally applied to dehumidification and radiation cold supply, and the temperature difference between supply water and return water is about 7-10 DEG C. A refrigeration cycle of a water chilling unit is realized with a non-azeotropic refrigerant, and good temperature matching of chilled water and the refrigerant in the heat exchanger is realized by means of the temperature slippage characteristic of the non-azeotropic refrigerant, so that the performance coefficient of the unit is increased.
Owner:SOUTHEAST UNIV

Gas-liquid countercurrent two-stage hydrocracking method

ActiveCN109777500AImprove temperature matchingReduce the amount of cold hydrogenTreatment with hydrotreatment processesChemistryNaphtha
The invention discloses a gas-liquid countercurrent two-stage hydrocracking method, which comprises the following steps: (1) using a fixed bed reactor, mixing feedstock oil with hydrogen, then firstlyenabling the mixture to enter a hydrofining reactor for carrying out desulfurization, denitrification and an aromatic hydrocarbon saturation reaction, and then enabling effluent to enter a flash tankso as to be subjected to gas-liquid separation; (2) enabling new hydrogen to enter a hydrocracking reactor from the bottom of the hydrocracking reactor, and enabling liquid phase effluent, obtained after separation of the flash tank, to enter the hydrocracking reactor from the top of the hydrocracking reactor so as to be subjected to a hydrocracking reaction, and enabling gas phase, obtained after separation of the flash tank, to separately enter different bed layer inlets of the hydrocracking reactor; (3) enabling effluent of the hydrocracking reactor to enter a separation system so as to besubjected to gas-liquid separation, recycling the separated gas as supplemental hydrogen, enabling the liquid phase product to enter a fractionating tower so as to be separated, carrying out fractionation in a the fractionating tower to obtain naphtha, jet fuel, diesel oil and tail oil. The method can effectively solve the problem of temperature matching of the refining and cracking reactors, reduces the consumption of cold hydrogen at an entrance of the cracking reactor, and increases the yield of the naphtha.
Owner:CHINA PETROLEUM & CHEM CORP +1

Thermoelectric supercooling cross-critical CO2 heat pump combined heating system

PendingCN110454851AReduce heat transfer temperature differenceReduce the irreversible loss of heat exchangeHeat pumpsCompression machinesEngineeringGas cooler
The invention discloses a thermoelectric supercooling cross-critical CO2 heat pump combined heating system. An outlet of an evaporator is connected with an inlet of a compressor; an outlet of the compressor is connected with an inlet of the working medium side of a gas cooler; an outlet of the working medium side of the gas cooler is connected with an inlet of the cold end of a thermoelectric supercooling device; an outlet of the cold end of the thermoelectric supercooling device is connected with an inlet of a throttling valve; an outlet of the throttling valve is connected with an inlet of the evaporator; a heating water return outlet is connected with an inlet of the thermal end of the thermoelectric supercooling device; an outlet of the thermal end of the thermoelectric supercooling device is connected with an inlet of the heat exchange fluid side of the gas cooler; an outlet of the heat exchange fluid side of the gas cooler is connected with an inlet of a mixing tank; and an outlet of the mixing tank is connected with a heating water return inlet. According to the system, the throttling loss is reduced to a greater extent, the high pressure of CO2 operation is further reduced,the overall system efficiency of a CO2 heat pump is improved, the compression ratio of the compressor is reduced, the isentropic efficiency is improved, and the service life of the compressor is prolonged.
Owner:TIANJIN UNIV OF COMMERCE

ORC (organic Rankine cycle) power generation system based on series connection of multistage evaporators

InactiveCN103195518AReduce defects with large irreversible lossesAvoid differential pressureSteam engine plantsOrganic Rankine cycleEngineering
The invention discloses an ORC power generation system based on series connection of multistage evaporators. The system comprises n evaporators , wherein the n evaporators are connected in series sequentially on a heat source side; a heat source fluid enters a first evaporator, is discharged from a last evaporator and is recharged to the underground; a working medium side of each evaporator is connected to n inlets of a steam turbine; an outlet of the steam turbine is sequentially connected with a preheater and a condenser in series; a working medium enters the preheater and the condenser, and then enters the other side of the preheater again and exchanges heat with exhaust steam exhausted by the steam turbine after working; the working medium flowing out of the preheater enters n working medium pumps in a parallel connection manner, and the n working medium pumps are connected to the n evaporators correspondingly, so that the closed cycle of the working medium is formed; a cold source side of the condenser is connected to a cooling water circulation system; a plurality of evaporator heat source sides are in series connection; and the working medium side is directly connected with the steam turbine in parallel, so that the defect that a single evaporator in a conventional ORC system is irreversible and has large loss is overcome, and the utilization efficiency and the technical economy of the system are improved.
Owner:TIANJIN UNIV

Triangular cycle and Rankine cycle combined waste heat recovery system and method thereof

The invention discloses a triangular cycle and Rankine cycle combined waste heat recovery system and a method thereof. The waste heat recovery system comprises working medium pumps, evaporators, expansion machines and condensers. In a triangular cycle, a working medium enters the high-temperature cycle evaporator, absorbs heat, always maintains a liquid state, and then, enters the expansion machine to act, and waste steam after acting preheats a low-temperature working medium in a Rankine cycle in the high-temperature cycle condenser; and in the Rankine cycle, the working medium enters the high-temperature cycle condenser, is in heat exchange with waste steam in the triangular cycle, then, enters the low-temperature cycle evaporator, is in counterflow heat exchange with low-temperature tail gas which is already in heat exchange with the high-temperature working medium in the high-temperature cycle, and then, enters the low-temperature cycle expansion machine to act. According to the triangular cycle and Rankine cycle combined waste heat recovery system, the working medium isothermal heat absorption process in the traditional Rankine cycle in the high-temperature cycle evaporator can be eliminated in the triangular cycle, the temperature matching problem between a heat source and the working mediums is solved, energy loss of the system is reduced, and efficient recycling of waste heat of automobile tail gas is facilitated.
Owner:ZHEJIANG UNIV

Air source transcritical CO2 heat pump and multi-melting-point phase change heat storage coupling heating system

The invention discloses an air source transcritical CO2 heat pump and a multi-melting-point phase change heat storage coupling heating system. The multi-melting-point phase change heat storage coupling heating system comprises a CO2 air source heat pump machine set, a first variable frequency pump, a high-melting-point phase change heat storage device, a user, a second variable frequency pump, a low-melting-point phase change heat storage device and a plurality of electromagnetic valves, wherein the secondary heat exchange side of a CO2 transcritical circular heat pump heating system is combined with the multi-melting-point phase change heat storage device; the low-melting-point phase change heat storage device is used for absorbing waste heat of return water, so that the temperature of the return water is reduced, and then the temperature of a working medium before a throttling valve and the throttling loss are reduced, thereby causing the temperature glide in the CO2 exothermic process to be in temperature matching with hot water very well and giving full play to the unique advantages of the CO2 transcritical circular heat pump heating system. In addition, when the peak value of electric power or the heat supply efficiency of the heat pump is relatively low, the system is switched into a heat release mode, and the heat of the phase change device is used for heat supply. The multi-melting-point phase change heat storage coupling heating system provided by the invention has the beneficial effects that the multi-melting-point phase change heat storage coupling heating system can operate and be controlled at different period of time during wave crest and wave trough of electric power, and then the comprehensive utilization performance of the heat pump machine set is improved.
Owner:XI AN JIAOTONG UNIV

Lubricating oil base oil production method

The present invention discloses a lubricating oil base oil production method. According to the lubricating oil base oil production method of the present invention, a wax oil raw material and hydrogen gas are mixed and then sequentially pass through at least two hydrogenation reaction zones connected in series, wherein each hydrogenation reaction zone sequentially comprises a composite catalyst bed layer filled with a hydrodewaxing catalyst and a hydrocracking catalyst in a mixed manner and a hydrodewaxing catalyst bed layer according to the material flowing direction, and the reaction effluent obtained from the last hydrogenation reaction zone is subjected to separation and fractionation to obtain the lubricating oil base oil, the white oil and other products. With the method of the present invention, the temperature decrease during the hydrodewaxing process and the temperature increase during the hydrogenation process are subjected to reasonable combination utilization, such that the low freezing point lubricating oil base oil is produced while the viscosity index is increased, the hot spot temperature of the device is reduced, and the operation period is prolonged; and the cold hydrogen consumption or the heating furnace fuel gas loss is reduced, and the operating cost is saved.
Owner:CHINA PETROLEUM & CHEM CORP +1

Power and cold air combined supply system driven by medium and low temperature heat source

The invention discloses a power and cold air combined supply system driven by a medium and low temperature heat source. The power and cold air combined supply system comprises a medium and low temperature heat source circulation system, an LNG cold energy utilization circulation system, a Kalina circulation system, an organic Rankine circulation system, an external ejection type refrigeration circulation system and an internal ejection type refrigeration circulation system; the Kalina circulation system is coupled with the medium and low temperature heat source circulation system through a boiler and a superheater; the organic Rankine circulation system is coupled with the medium and low temperature heat source circulation system through an ORC preheater, and the organic Rankine circulation system is coupled with the Kalina circulation system through an ORC evaporator; an ejection flow of an ejector of the internal ejection type refrigeration circulation system is medium-high pressure ammonia gas led out from a certain position in the middle of a turbine in the Kalina circulation system, and the ejected flow is a two-phase flow of an outlet of a first evaporator; and an ejection flow of an ejector of the external ejection type refrigeration circulation system is ammonia water at an outlet of a condenser in the Kalina circulation system, and an ejected flow is a two-phase mixture at an outlet of an evaporator.
Owner:SHANDONG UNIV

Variable-concentration directly-heated type heat pump water heater with flash evaporators and working method thereof

The invention provides a variable-concentration directly-heated type heat pump water heater with flash evaporators and a working method thereof. The variable-concentration directly-heated type heat pump water heater with the flash evaporators comprises a main circulation loop, an air supplementing branch and a concentration adjusting branch, and the main circulation loop is formed by connecting acompressor, a condenser, a high-pressure liquid storage device, a subcooler, a first expansion valve, the flash evaporator, a first stop valve, a third stop valve, a second expansion valve and an evaporator; the air supplementing branch is provided with the flash evaporator and a second stop valve which are connected in sequence; and the concentration adjusting branch is formed by connecting a working medium supplementing expansion valve, a component separation and working medium storage tank, an air supplementing concentration adjusting valve and a liquid supplementing concentration adjustingvalve. According to the variable-concentration directly-heated type heat pump water heater, based on the principle of advantage complementation, enhanced vapor injection and working medium concentration adjusting technologies are comprehensively applied to the heat pump water heater, the low-temperature performance and annual comprehensive energy efficiency of the heat pump water heater can be remarkably improved, meanwhile, the applicable temperature range of the heat pump water heater is obviously widened, and the heat pump water heater further has the advantages of being simple in rectification structure, high in component separation efficiency, safe, reliable and the like.
Owner:ZHONGYUAN ENGINEERING COLLEGE

Absorption, compression and ejection composite cascade supercooling transcritical CO2 combined cooling and heating system

The invention provides an absorption, compression and ejection composite cascade supercooling transcritical CO2 combined cooling and heating system. The system is composed of a transcritical CO2 refrigeration cycle, an absorption, compression and ejection composite cascade supercooling cycle and a hot-end heat-supply cycle, the absorption, compression and ejection composite cascade supercooling cycle is subjected to cascade throttling depressurization, therefore, supercooling of two different evaporation pressures is realized, the CO2 fluid at the outlet of a CO2 gas cooler is subjected to twocontinuous cascade supercooling, so that better temperature matching is formed during the heat exchange process, and the heat transfer temperature difference is reduced, the heat exchange irreversible loss in a CO2 subcooling process is significantly reduced, the temperature of the CO2 fluid at the outlet of the gas cooler is reduced, the throttling loss of CO2 is reduced, the compression ratio of a compressor is reduced, the isentropic efficiency is improved, and then the COP of the system is improved. The combined cooling and heating system can be widely applied to various occasions needingrefrigeration or heating, such as refrigeration, medium-high temperature hot water making and heating.
Owner:TIANJIN UNIV OF COMMERCE

Direct heating type heat pump water heater with adjustable concentration and wide temperature zone and working method thereof

InactiveCN111964261AElevated circulating concentrationsGood temperature matchingFluid heatersHeat pumpsEngineeringDirect heating
The invention provides a direct heating type heat pump water heater with adjustable concentration and a wide temperature zone and a working method thereof. The water heater includes a main circulationloop, an air supplement branch and a concentration adjustment branch. The main circulation loop is provided with a compressor, a condenser, a high-pressure liquid accumulator, a subcooler, an economizer, a first expansion valve and an evaporator which are sequentially connected. The air supplement branch is provided with a second expansion valve, an economizer and a stop valve which are connectedsequentially. The concentration adjustment branch is composed of a working medium supplementary expansion valve, a component separation and working medium storage tank, an air supplement concentration regulating valve and a liquid supplement concentration regulating valve. The air jet enthalpy increase and working medium concentration adjustment technologies are comprehensively adopted, the significant improvement in the low-temperature performance of the heat pump water heater, significant expansion of the applicable temperature zone, and significant improvement in the overall energy efficiency throughout the year are simultaneously achieved. In addition, the water heater further has many advantages of simple distillation structure, high component separation efficiency, simple control, safety and reliability.
Owner:ZHONGYUAN ENGINEERING COLLEGE

Adsorption type refrigerating system and method based on cooking fume discharging equipment

The invention provides an adsorption type refrigerating system and method based on cooking fume discharging equipment. The refrigerating system comprises a desorption and adsorption device used for adsorption and desorption of a refrigerant, a heat releasing device and a heat absorbing refrigerating device. The desorption and adsorption device comprises an adsorption bed device and a smoke exhaust hood. The adsorption bed device comprises at least one adsorption bed and is arranged in the smoke exhaust hood, and the desorption and adsorption device is used for refrigerant adsorption and desorption. The heat releasing device is connected with the desorption and adsorption device and used for condensation of the refrigerant desorbed by the desorption and adsorption device. One end of the heat absorbing and refrigerating device is connected with the heat releasing device so as to receive the refrigerant output by the heat releasing device, and the other end of the heat absorbing and refrigerating device is connected with the desorption and adsorption device so as to provide the refrigerant for the desorption and adsorption device. The adsorption bed device of the adsorption type refrigerating system based on the cooking fume discharging equipment is combined with the smoke exhaust hood, heat gathering is achieved through the characteristics that a gas collecting hood (the smoke exhaust hood) is large in area and gets close to a heat source, and the equipment occupied space is saved.
Owner:上海东方延华节能技术服务股份有限公司

CO2 transcritical thermodynamic cycle electricity storage system and method

The invention discloses a CO2 transcritical thermodynamic cycle electricity storage system, which comprises a heat pump circulation loop, a heat storage unit and a cold storage unit, wherein the heat storage unit and the cold storage unit are connected to the heat pump circulation loop, the heat pump circulation loop converts a working medium in the heat pump circulation loop into a high-temperature and high-pressure supercritical state and sends the working medium into the heat storage unit, the heat storage unit is internally provided with multiple sections of heat storage media, and a high-temperature and high-pressure supercritical working medium enters the heat storage unit and sequentially exchanges heat with each section of the heat storage media at an approximately constant temperature difference, so that heat energy is stored in the heat storage media. The invention further provides an electricity storage method of the CO2 transcritical thermodynamic cycle electricity storage system. In the heat exchange process of the high-temperature-end cycle working medium and the heat storage medium, good temperature matching in the heat exchange process of the high-temperature-end cycle working medium and the heat storage medium is achieved through the segmented heat exchange technology of mass flow adjustment and phase change heat storage medium conversion, and the heat exchange efficiency and the overall efficiency of the electricity storage system are improved.
Owner:INST OF MECHANICS - CHINESE ACAD OF SCI

All-regenerative Brayton cycle and absorption refrigeration integrated power and cooling combined supply system

The invention discloses a full-heat-regeneration Brayton cycle and absorption type refrigeration integrated electricity and cooling combined supply system. The system comprises a supercritical carbon dioxide Brayton cycle power generation system, a pre-cooling-boiler coupling heat regeneration module and an absorption type electricity and cooling combined supply system. The supercritical carbon dioxide Brayton cycle system is combined with the absorption type electricity-cooling combined supply system, low-pressure high-temperature side outlet carbon dioxide waste heat of a low-temperature heat regenerator outlet is fully utilized, heat is provided for the absorption type electricity-cooling combined supply system in combination with the pre-cooling-boiler coupling heat regeneration system, low-temperature waste heat of the low-temperature heat regenerator outlet can be fully utilized, and the heat utilization rate of the low-temperature heat regenerator outlet is improved. And meanwhile, a large amount of cooling water and a precooler required by the Brayton cycle are omitted, the investment cost of the high-temperature heat regenerator and the low-temperature heat regenerator is reduced, and the power generation efficiency of the Brayton system is improved.
Owner:HEFEI GENERAL MACHINERY RES INST

CO2 refrigerating and heating integrated system capable of performing mechanical assisted super-cooling through non-azeotropic working medium

The invention discloses a CO2 refrigerating and heating integrated system capable of performing mechanical assisted super-cooling through a non-azeotropic working medium. Non-azeotropic mixed steam compression cycle is combined with CO2 trans-critical cycle; the non-azeotropic working medium has temperature glide in a phase-change process; one path of return water flows through a condenser which is assisted by the non-azeotropic working medium to circulate, the other path of return water flows through a CO2-cycle gas cooler to heat, temperature difference of inlets and outlets of two paths ofwater is relatively small, and relatively good temperature matching is formed between an assisted-cycle non-azeotropic mixed working medium condensing process and a CO2 fluid cooling process. Very good temperature matching is formed between a non-azeotropic refrigerant evaporating process and a trans-critical CO2 fluid cooling process, heat-exchange irreversible loss in the condenser, a gas coolerand a cooling evaporator can be greatly reduced through a combined heating system, compressor input power can be reduced by recycling expansion work through an expanding machine, and efficient operation of CO2 refrigerating and heating integrated system is guaranteed.
Owner:TIANJIN UNIV OF COMMERCE

Non-azeotropic working medium dual-stage organic flash evaporation circulation system and heat energy recovery method thereof

The invention discloses a non-azeotropic working medium dual-stage organic flash evaporation circulation system and a heat energy recovery method thereof, and belongs to the field of energy recovery.A working medium exchanges heat with a waste heat medium in a heat exchanger after being pressurized by a working medium pump, and enters a high-pressure-stage gas-liquid separator after being throttled by a first throttle valve; a saturated steam after high-pressure-stage flash evaporation enters a high-pressure-stage turbine to do work through expansion, and saturated liquid is throttled again through a second throttle valve to change into a gas-liquid mixture; the gas-liquid mixture and exhaust gas are mixed in a high-pressure-stage mixer, and then enter a low-pressure-stage gas-liquid separator together; saturated steam after the low-pressure-stage flash evaporation enters a low-pressure-stage turbine to do work through expansion, saturated liquid is throttled through a third throttledvalve to change to a gas-liquid mixture, and the gas-liquid mixture and the exhaust gas are mixed in a low-pressure-stage mixer; and the gas-liquid mixture and the exhaust gas are jointly cooled in acondenser. The temperature matching between the circulation and a cold source is improved, the exergy loss caused by single-stage OFC direct throttling is reduced, the system efficiency is improved,and the stepwise efficient use of medium and low temperature thermal energy is realized.
Owner:YUNNAN UNIV

Jet booster two-stage super-cooling trans-critical CO2 dual-temperature system and application

The invention provides an ejector booster two-stage super-cooling trans-critical CO2 dual-temperature system and application. The ejector booster two-stage super-cooling trans-critical CO2 dual-temperature system comprises an ejector, booster, and dual-supercooler series mechanical super-cooling cycline and a trans-critical CO2 dual-temperature-region cycle, which can mutually exchange heat; the trans-critical CO2 dual-temperature-region cycle comprises a CO2 low-temperature-stage evaporator, an outlet of the CO2 low-temperature-stage evaporator sequentially communicates with a CO2 low-pressure-stage compressor, a CO2 medium-pressure-stage compressor, a CO2 high-pressure-stage compressor, a heating medium side of a CO2 gas cooler, a heating medium side of the medium-temperature-stage cooling evaporator, a heating medium side of a low-temperature-stage cooling evaporator, a medium-temperature-stage gas-liquid separator, a low-temperature-stage gas-liquid separator and an inlet of a CO2low-temperature-stage evaporator. The ejector booster two-stage super-cooling trans-critical CO2 dual-temperature system can reduce gas exhaust pressure of the compressor, reduces a pressure ratio ofthe CO2 compressor, improves isentropic efficiency, and prolongs the service life of the compressor.
Owner:CHINA NAT ENERGY REFINING & CHEM ENG CO LTD

Work and coldness co-production system and method of recovering working medium effective ingredient refrigeration

The invention discloses a work and coldness co-production system and a method of recovering working medium effective ingredient refrigeration and relates to the medium and low temperature heat source using technical field. The work and coldness co-production system and the method of recovering working medium effective ingredient refrigeration are driven by medium and low temperature heat source and used ammonia water mixture as a working medium, organically integrates ammonia water working subcycle with ammonia water absorption refrigeration subcycle, achieves co-production of work and coldness, and improves use efficiency of the medium and low temperature source. The work and coldness co-production system and the method of recovering working medium effective ingredient are mainly characterized in that: firstly, gradient use of heat is achieved according to a temperature counterpart principle, a high temperature part of an outer heat source is used for work subcycle, a low temperature part of the outer heat source is used for refrigeration, and working subcycle heat extraction is also used for refrigeration subcycle; secondly, recovering power subcycle can further be used due to ammonia working medium containing turbine exhaust of the recovering power subcycle.
Owner:INST OF ENGINEERING THERMOPHYSICS - CHINESE ACAD OF SCI
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