995 results about "Heat recirculation" patented technology

An aqueous stream cleaning system including a circulation pump to receive a waste fluid and / or a concentrated liquid bottoms stream, and expel a circulation stream. The aqueous stream cleaning system can also include a primary heat exchanger to receive the circulation stream from the circulation pump. The primary heat exchanger can have a plurality of heat exchange plates that define an internal surface area for heat transfer from a distillate stream to the circulation stream to produce a cooled distillate stream and a heated circulation stream. The plurality of heat exchange plates can be spaced to facilitate free flow of solids in the circulation stream between the plurality of heat exchange plates. A mass flow rate and pressure of the circulation stream can be configured to minimize build-up of solids in the primary heat exchanger. The aqueous stream cleaning system can further include an evaporation unit to receive the heated circulation stream from the primary heat exchanger. The distillate stream is formed when steam in the heated circulation stream evaporates in the evaporation unit, and the concentrated liquid bottoms stream is formed from a portion of the heated circulation stream that does not evaporate.

The invention belongs to the technical field of refrigerants, and provides a mixed refrigerant for replacing R290 and a preparation method and application thereof, the mixed refrigerant comprises a first component, a second component and a third component; the first component is trans-1, 2-difluoroethylene, the second component is 2, 3, 3, 3-tetrafluoropropene, and the third component is trifluoromethyl methyl ether; compared with R290 refrigerants in the prior art, the mixed refrigerant has the advantages that flammable and explosive components do not exist, and high-risk combustible gas clusters cannot be formed due to density layering after leakage, so that the mixed refrigerant has high safety performance, and the safety level can be not lower than A2L; the mixed refrigerant has the environment-friendly characteristic of low GWP, the GWP is smaller than or equal to 150, and the environment-friendly requirement is met; the thermophysical property and the refrigeration and / or heating cycle performance of the mixed refrigerant are similar to or better than those of R290; the mixed refrigerant can be used for directly replacing an R290 refrigerant.

The invention relates to a liquid air energy storage and terrestrial heat coordinated underground space air regulation and control system and method. Comprising a first-stage compressor, a second-stage compressor, a third-stage compressor, an expansion refrigerator, a first-stage compression heat exchanger, a second-stage compression heat exchanger, a third-stage compression heat exchanger, a cold box, a separator, a liquid air storage tank, a cryogenic pump, an evaporator, a cold storage circulating pump, a cold storage box, a compression heat exchange circulating pump, a compression heat storage box, a first heater, a second heater and a third heater. The system comprises a first air expander, a second air expander, a third air expander and a generator. The regeneration heater is used for guiding the compression heat generated by the compressor into the regeneration heater for regeneration and / or guiding the geothermal energy output by the geothermal energy output end into the regeneration heater for regeneration; the rotary wheel dehumidification device is used for performing cryogenic drying on the wet air; the fresh air processing unit is composed of a fresh air filter, a regeneration fan, a regeneration filter and an air supply fan.

The invention provides a pot support, and relates to the technical field of gas cooks.The pot support mainly comprises a ring body, and the outer edge of the ring body is higher than the inner edge of the ring body so that a combustion area can be defined; an upper cavity and a lower cavity which are stacked and independent are formed in the ring body; the lower cavity is a closed cavity; an air inlet hole and an air outlet hole which are communicated with the interior and exterior of the upper cavity are formed in the cavity wall of the upper cavity to form a channel for high-temperature gas to flow; the air inlet and the air outlet are arranged away from each other; the air outlets face the through hole in the bottom of the ring body. According to the embodiment provided by the invention, part of generated high-temperature gas is sucked into the upper cavity from the air inlet holes in the high position, the high-temperature gas flows along the upper cavity, heat of the high-temperature gas is conducted through the cavity wall, the temperature of the whole pot support is greatly increased, the heated pot support directly conducts efficient heat conduction heating on a pot, and the heating efficiency is improved. And the high-temperature gas finally flows downwards and flows out from the gas outlet hole, and flows upwards and is sucked into the upper cavity, so that heat circulation is formed, and the overall heat efficiency is remarkably improved.

The utility model discloses a multi-system water chilling unit which comprises at least two heat exchange systems, at least two waterway systems and a combined heat exchanger, and the heat exchange systems can be combined to form or respectively form an independent heat exchange circulation loop by switching the serial or parallel connection state and the opening or closing state of the combined heat exchanger; the water path system can be combined to form or respectively form an independent water circulation loop, so that the heating or refrigerating capacity of the unit is obviously increased; different heat exchange circulation loops are switched and controlled by adjusting refrigerant flowing paths between the multiple heat exchange systems and the combined heat exchanger, and different water circulation loops are switched and controlled by adjusting water medium flowing paths of the multiple water path systems. Therefore, after the water chilling unit is installed, different operation modes can be selected and switched according to different heat or cooling capacity requirements, hot water or cold water with the corresponding capacity and temperature is produced, the heating or cooling capacity of the unit is matched with the actual requirement, the whole equipment or part of elements do not need to be replaced, cost is low, and maintenance is convenient.

The invention provides a porous medium combustor for stable combustion of ultralow-calorific-value gas, belongs to the technical field of combustors, and solves the problems that an existing combustor is low in heat recycling efficiency and air is not fully preheated before entering a combustion area. The combustor comprises a shell, a gradually-shrunk porous medium layer, a stable-combustion porous medium layer, a gradually-expanded porous medium layer, a premixing chamber, a fuel channel and an oxidizing agent channel, and the gradually-shrunk porous medium layer, the stable-combustion porous medium layer and the gradually-expanded porous medium layer are all located in the shell and are sequentially arranged from top to bottom; the premixing chamber is communicated with the lower part of the divergent porous medium layer; an outlet of the fuel channel is communicated with the premixing chamber; the oxidant channel surrounds the stable combustion porous medium layer and the divergent porous medium layer and is spirally arranged on the shell, an inlet of the oxidant channel is located above the stable combustion porous medium layer, and an outlet of the oxidant channel is communicated with the premixing chamber. The combustible limit of the low-heating-value fuel gas can be widened, stable and efficient utilization of the ultralow-heating-value fuel gas is achieved, and the heat recycling efficiency is improved.

The utility model relates to the technical field of acid pickling waste liquid resourceful treatment and regeneration, in particular to a tail gas waste heat utilization system of a mixed acid waste liquid treatment system, which is used for treating mixed acid waste liquid and discharging high-temperature tail gas and comprises a first heat exchanger, a second heat exchanger and a refrigerating mechanism. A first heat exchange circulating water path is arranged between the first heat exchanger and the refrigerating mechanism; the first heat exchanger provides a heat source for the refrigerating mechanism by using tail gas heat and reduces the water temperature of the first heat exchange circulating water path by means of the refrigerating mechanism; a second heat exchange circulating water path is arranged between the second heat exchanger and the refrigerating mechanism. The second heat exchanger is further connected to a circulating pipeline of the mixed acid waste liquid treatment system so as to reduce the temperature of circulating liquid. Through the tail gas waste heat utilization system, flue gas waste heat of the mixed acid waste liquid treatment system is effectively recycled, and energy waste is reduced; and the second heat exchanger reduces the circulating liquid temperature of the mixed acid waste liquid treatment system and improves the oxidation efficiency of the flue gas.

The invention discloses a heat pump unit with an energy recovery function, and belongs to the technical field of heat pumps, the heat pump unit comprises a machine shell, a heat circulation mechanism, a fan, a condensation box and a waste heat recovery box are arranged in the machine shell, and a circulation conveying mechanism and a driving mechanism are arranged on one side of the waste heat recovery box; the circulating conveying mechanism comprises a compression box and a piston plate; the driving mechanism comprises a driving motor, a driving shaft, a guide rail and a rotating shaft. By integrating the heat circulation mechanism, the waste heat recycling box and the circulation conveying mechanism, the energy utilization efficiency is remarkably improved, in the operation process of the heat pump unit, the compressor compresses a low-temperature and low-pressure gas-state refrigerant into high-temperature and high-pressure gas, the condenser transmits heat to water in the condensation box, and therefore the heat pump unit is cooled. Meanwhile, a waste heat recovery box further recovers residual heat of the refrigerant, gradient utilization of energy is achieved, a fan enhances air circulation and improves heat exchange efficiency, and a temperature sensor and a controller dynamically adjust system operation parameters to ensure that the temperature of hot water is stable.

The invention belongs to the technical field of hydrogen energy, and particularly relates to a solid hydrogen storage system with two charging and discharging ends and a working method.The solid hydrogen storage system comprises at least two independent solid hydrogen storage units, and each solid hydrogen storage unit independently communicates with an upstream hydrogen supply pipeline through a first valve set and independently communicates with a downstream hydrogen using pipeline through a second valve set; each solid hydrogen storage unit is selectively communicated with the thermal circulation loop or the cold circulation loop through a third valve group; the first valve group, the second valve group and the third valve group are controlled, so that when the upstream hydrogen supply pipeline has a hydrogen supply demand and the downstream hydrogen use pipeline has a hydrogen use demand, the first solid hydrogen storage unit is configured to be in a hydrogen charging mode, and meanwhile, the second solid hydrogen storage unit is configured to be in a hydrogen discharging mode; the solid hydrogen storage unit in the hydrogen charging mode is communicated with the upstream hydrogen supply pipeline and the cold circulation loop for charging hydrogen, and the solid hydrogen storage unit in the hydrogen discharging mode is communicated with the downstream hydrogen supply pipeline and the hot circulation loop for discharging hydrogen.

The invention discloses an efficient thermal cycle drying device for producing flaky ammonium bifluoride, and relates to the technical field of ammonium bifluoride production. Comprising a machine body, an exhaust pipe and an air inlet sleeve, a first shell and a second shell are sequentially mounted at the upper end of the machine body from left to right, an air inlet cavity is formed in the bottom of the inner side of the machine body, and a mounting cylinder is connected to the upper end of the air inlet cavity through a spring; through cooperation of a mounting cylinder, a movable cylinder, a scraping plate and a first adjusting assembly, when materials are subjected to traditional one-way vibration blowing heat exchange, the materials are thrown and turned in the other direction to increase the drying uniformity, meanwhile, the air flow pressure of an exhaust hole is correspondingly adjusted, and the heat exchange drying effect is improved; and through cooperation of the movable barrel and the second adjusting assembly, when materials with the large water content and the large feeding amount are dried, the moving speed of the materials is increased, meanwhile, the air flow pressure of the exhaust holes is correspondingly adjusted, and the heat exchange drying effect is improved.

The present invention provides a power plant waste heat recovery system and method, which simultaneously recovers a wide range of waste heat from power plants and also implements cascade recycling of waste heat from power plants. The present invention simultaneously recycles all waste heat from thermal power plants, including four types of waste heat: flue gas waste heat, circulating water waste heat, furnace wall waste heat, and slag waste heat. In addition, according to the different characteristics of waste heat, different heat pumps and different heat exchangers are selected to efficiently recover all recoverable waste heat, thereby improving the energy conversion efficiency of the power plant. The present invention designs a cascade recycling of waste heat from power plants, including three recycling methods: a low-pressure steam turbine generator set, a low-boiling-point working fluid generator set, and a heating pipeline. On the one hand, the present invention improves the applicability of the power plant waste heat recovery system, and is applicable to different types of thermal power plants, as well as to the effects of different seasons and environmental temperature factors on various waste heat. On the other hand, by comparing and matching the temperature and pressure set values ​​of the recycling equipment with the measured values, the waste heat is maximized and waste heat is avoided.

According to the transformer cooling system provided by the invention, transformer oil led out from the transformer main body sequentially flows into the circulating oil pump and the Venturi tube through the oil outlet pipe. The circulating oil pump can provide strong power for circulation of the transformer oil, and the Venturi tube enables the transformer oil to be in a turbulent flow state. And then, the transformer oil in the turbulent flow state enters the heat dissipation device, and efficient heat dissipation treatment is carried out. And the transformer oil subjected to heat dissipation stably flows back to the transformer main body through the oil return pipe, so that a complete heat dissipation cycle is formed. In the system, through cooperation of the circulating oil pump and the Venturi tube, the circulating flowing speed of transformer oil is remarkably increased, the transformer oil can pass through the heat dissipation device at a higher speed, a boundary layer between hot oil and the surface of a heat medium channel of the heat dissipation device is effectively damaged, and therefore the heat transfer efficiency is improved, and the heat dissipation efficiency is improved. Therefore, heat can be conducted to the surface of the heat dissipation device more quickly, and the heat dissipation efficiency of the whole heat dissipation system is further improved.

The utility model relates to a triple-cycle high-salinity wastewater low-temperature scraper drying system which comprises a roller scraper dryer, a steam condensation chamber, a condensed water tank and a vacuum pump, the vacuum pump vacuumizes the drying cavity through the condensate water tank and the steam condensation chamber. The first heat exchange cycle is suitable for exchanging heat absorbed by the steam condensation chamber to the third heat exchange cycle; the second heat exchange cycle is suitable for exchanging heat of the third heat exchange cycle to the water jacket; and the heat exchange ends on the two sides of the third heat exchange cycle are connected with the first heat exchange cycle and the second heat exchange cycle correspondingly. The three heat exchange cycles work cooperatively, the heat of the first heat exchange cycle is reduced, the heat provided for the second heat exchange cycle by the third heat exchange cycle is reduced, and the hot water in the second heat exchange cycle can still heat the materials in the drying cavity by exceeding the boiling point rise through the auxiliary heat, so that the low water content of the dry materials is effectively ensured.

The utility model relates to the technical field of chemical production, particularly discloses a turbidity control system for chemical cooling circulating water, and solves the problem that the cooling effect of chemical equipment is finally influenced due to the fact that the circulating water is easily polluted by a chemical cleaning agent or the environment in the process of cooling the chemical equipment by the circulating water for a long time at present. According to the system, a plurality of cut-off control valves are arranged at water inlet and outlet pipelines of a filter, a liquid level meter is additionally arranged at the top of a slurry tank, and a plurality of control valves are arranged between the slurry tank and a press filter, so that circulating water is further filtered through the additional filter when being subjected to conventional cooling heat exchange circulation; the cleanliness of the cooling water entering the circulating water tank is further improved; and the slag slurry water backwashed by the filter is further filtered by the press filter, so that the filtered slag slurry water is pumped into the circulating water tank again, the turbidity of the cooling circulating water is effectively reduced, and the recycling rate of the filtered slag slurry water is improved.

The utility model discloses a refrigeration structure with an anti-deformation pipeline and an ice cream machine using the refrigeration structure. The refrigeration structure comprises a freezing cylinder, a compressor, a heat exchanger, a refrigeration circulating pipeline and a heat exchange circulating pipeline, the compressor is provided with a condensation outlet, a condensation inlet, a heat exchange inlet and a heat exchange outlet; the refrigeration circulation pipeline comprises a capillary tube, a condensation tube and an air return tube which are sequentially communicated; the heat exchange circulation pipeline comprises a cold source input pipe and an exhaust pipe. According to the refrigeration structure, an air return pipe is arranged in a refrigeration circulation pipeline, an exhaust pipe is arranged in a heat exchange circulation pipeline, and a plurality of sections of bent structures are arranged in the air return pipe and the exhaust pipe respectively, so that anti-bending structures are formed. Due to the fact that the air return pipe and the exhaust pipe are of a bent structure, the air return pipe and the exhaust pipe can bear drawing force and deform to a certain degree when vibration occurs in the transportation process or collision and falling occur in the carrying process, and therefore the air return pipe and the exhaust pipe can bear influences caused by vibration, and the problem that the air return pipe and the exhaust pipe are damaged is solved.

The invention belongs to the technical field of salt spray tests, and particularly relates to a test device and method for simulating hot corrosion of an engine turbine blade material, and the method comprises the following steps: after a sample is cleaned and dried, a nozzle is controlled by a mechanical arm to atomize a saturated salt solution, and the saturated salt solution is precisely sputtered to the surface of the sample preheated to 300-500 DEG C to form a uniform salt film; the sample is placed in a heating furnace at the temperature of 600-1000 DEG C to be subjected to heat preservation for 50-55 min and then cooled by compressed air for 5-10 min, and cold and hot circulation A corrosion kinetic curve is drawn based on the unit area weight increment, corrosion products are removed through a molten alkali electrolysis method, and the hot corrosion rate is calculated. The device comprises a groove type test bed with a high-temperature-resistant coating, a slit type nozzle driven by a mechanical arm, an infrared heating device and a cold and hot circulation system. According to the method, the salt film is deposited through precise position control of the mechanical arm, the cold and hot alternating working condition is simulated, the problems that a traditional salt coating method is not uniform and a salt leaching method is distorted in environment are solved by combining corrosion dynamics and microscopic characteristic analysis, and scientific evaluation of the corrosion resistance of the aero-engine blade material is achieved.

The utility model relates to the technical field of battery thermal management, and discloses a battery thermal management device and a battery pack, and the battery thermal management device comprises a plurality of heat pipes, a battery cell and a cooling piece. According to the battery heat management device with the structure, in a cooling mode, a liquid working medium in the evaporation section at the bottom of the heat pipe is heated and evaporated into a gaseous working medium, the gaseous working medium rises to the condensation section at the top of the heat pipe, the gaseous working medium is in contact with a low-temperature wall surface of the condensation section to be condensed into the liquid working medium, and the liquid working medium flows back to the condensation section at the bottom of the heat pipe by gravity; and heat exchange circulation is achieved. The transition section, the condensation section and the evaporation section of the heat pipe are all in contact with the battery cell, so that the heat exchange area is greatly increased, the heat exchange amount is increased, and the cooling effect of the battery cell can be remarkably improved. The arrangement number of the cooling plates can be reduced, so that the arrangement of the cooling pipelines can be simplified, the occupied space of the cooling plates and the cooling pipelines can be reduced, and the volume utilization rate and the mass energy density of the battery thermal management device and the battery pack can be improved.

The utility model discloses a hot air penetration type drying system for wet spunlace, which comprises a wall frame, a thermal cycle air supplement adjusting device and a circulating fan, and an upper-layer flow guide air plate, a rotary drum drying net and a lower-layer flow guide air plate are arranged in the wall frame; the upper-layer flow guide air plate is located above the rotary drum drying net, the lower-layer flow guide air plate is located below the rotary drum drying net, and the thermal cycle air supplement adjusting devices are arranged at an inlet and an outlet of the drying oven respectively. Due to the unique penetrating type design, hot air can directly act on the surfaces of materials, the drying time is greatly shortened, and meanwhile energy consumption is reduced.

A coupling system for liquefied natural gas re-gasification and liquid air energy storage. The coupling system comprises a liquefied natural gas re-gasification system and a liquid air energy storage system. The liquefied natural gas re-gasification system comprises: a heat exchanger-natural gas (HX-NG) connected to a liquefied natural gas re-gasification path. The liquid air energy storage system comprises: a heat exchanger-charge (HX-C) connected to a main gas liquefaction path, a heat exchanger-discharge (HX-DC) connected to a liquefied main gas re-gasification path, and a cold dewar (CD), wherein a first heat exchange cycle where cold energy exchange is performed with a first heat exchange medium is formed between the heat exchanger-natural gas and the heat exchanger-charge; and a second heat exchange cycle where cold energy exchange is performed with a second heat exchange medium is formed among the heat exchanger-charge, the cold dewar and the heat exchanger-discharge. In the first heat exchange cycle, a hot end of the heat exchanger-natural gas is connected to a hot end of the heat exchanger-charge, and a cold end of the heat exchanger-natural gas is connected to a cold end of the heat exchanger-charge; and in the second heat exchange cycle, hot ends of the heat exchanger-charge, the cold dewar and the heat exchanger-discharge are connected, and cold ends of the heat exchanger-charge, the cold dewar and the heat exchanger-discharge are connected. In the present invention, regardless of whether the liquid air energy storage system is in a charging working state, a standing working state or a discharging working state, effective coupling utilization of cold energy and heat energy between the liquid air energy storage system and the liquefied natural gas re-gasification system can be realized, improving the effective coupling utilization rate of cold energy and heat energy between the systems.

The invention discloses an absorption refrigeration system based on combined driving of solar energy and waste heat of a data center. The absorption refrigeration system comprises a multi-energy complementary heat collection circulation module and an absorption refrigeration circulation module. The multi-energy complementary heat collection circulation module comprises a solar heating unit, a liquid cooling cabinet and a plate heat exchanger. And the solar heating unit and the liquid cooling cabinet are respectively connected with the plate heat exchanger. And the absorption refrigeration cycle module is connected with the multi-energy complementary heat collection cycle module. The absorption type refrigeration cycle module comprises an absorption type refrigeration cycle generator, a gas-liquid separator, a condenser, an evaporator, a mixer, an absorber and a solution exchanger. And the absorption refrigeration cycle generator is connected with the plate heat exchanger and the gas-liquid separator. And the gas-liquid separator is connected with the condenser and the solution exchanger. And the condenser is connected with the evaporator. The mixer is connected with the solution exchanger, the evaporator and the absorber. And the absorber is connected with the absorption refrigeration cycle generator. Dependence on external energy can be reduced, and the energy utilization efficiency is improved.

The invention discloses a variable-capacity air fryer convenient to operate. Comprising a base, a guide rail assembly vertically arranged on the side of the base, a sliding seat assembly in sliding fit with the guide rail, a heating machine head arranged on a sliding seat, an elastic reset piece connected with the guide rail and the sliding seat, an elastic locking assembly arranged on the sliding seat, an external first handle and at least two pot bodies. The guide rail is provided with a plurality of gear lock holes and a sliding groove, and the first handle is connected with the sliding seat through the sliding groove and can drive the sliding seat to ascend and descend and enable the locking assembly to be inserted into the corresponding lock hole so as to lock the height of the machine head. And the pot body can be placed on the base and covers the machine head. The structure realizes quick adjustment of the machine head, adapts to pot bodies with different capacities, does not need to disassemble the machine head, and is convenient to operate, sanitary, safe, and good in sealing performance and heat cycle effect.

The invention provides a segmented heat control welding method and system for a dual-phase steel thick-wall component, and relates to the technical field of welding. The method comprises the steps that a segmented unit planning set is constructed; generating a segmented unit multi-source synchronous data set; constructing a welding thermal cycle characteristic parameter set; generating a welding control constraint set; obtaining a segmented heat input deviation instruction set; generating a welding process parameter adjusting instruction; and according to the actual welding seam structure performance in the long-term welding process, a parameter optimization algorithm is adopted to optimize the adjustment process, and continuous updating of the segmented heat control welding model is achieved. The technical problems that in the prior art, heat input control is extensive, temperature field monitoring is not comprehensive, technological parameter adjustment lags behind, and quantitative bases are lacked are solved.

The embodiment of the invention provides a heat pump system and a control method and device thereof and a storage medium, and belongs to the technical field of air conditioners, and the heat pump system comprises a heat exchange terminal, a water storage tank, a first heat pump set, a switching device and a second heat pump set; the first heat pump set comprises a main water outlet. The switching device is connected with a main water outlet of the first heat pump set, the heat exchange terminal and the water storage tank. The control method comprises the steps that when a heating instruction and a water heating instruction are received, the first heat pump set and the second heat pump set are controlled to work, a total water outlet of the first heat pump set communicates with a water inlet of the water storage tank, and when it is detected that a heat pump machine meets the defrosting condition, the first heat pump set and the second heat pump set are controlled to work; detecting whether a priority instruction exists or not; and when the priority instruction exists and the heat pump machine meeting the defrosting condition meets the preset condition, the main water outlet of the first heat pump set is switched to be communicated with the water inlet of the heat exchange terminal, and therefore heating and water heating can be conducted at the same time, and temperature fluctuation caused by defrosting is relieved.

A waste heat recycling device of a molecular sieve oxygenerator comprises an air compressor A, an air compressor B, a circulating water tank, a heat preservation water tank and a cooling tower, the air compressor A and the air compressor B are connected with a heat exchanger A and a heat exchanger B through circulating pipelines respectively, a thermostatic valve A and a thermostatic valve B are arranged on the circulating pipelines respectively, and the heat exchanger B is connected with the heat exchanger A and a heat exchanger C; the circulating water tank is connected with the heat exchanger A and the heat exchanger C, and a water pump A is arranged on a pipeline connected with the heat exchanger A. The circulating water tank is connected with the cooling tower so that the heat dissipation capacity of the air compressor at the high temperature in summer can be improved, the air compressor is prevented from being shut down at the high temperature, the PLC automatically switches the waste heat recovery mode and the cooling tower heat dissipation mode according to the water temperature priority, and energy waste is avoided. Multiple heat exchangers are adopted for heat exchange, circulating water and user water are isolated from each other, and scale and domestic water pollution caused by high temperature are avoided, so that energy needed by working of the cooling tower is saved, domestic hot water and energy needed by air conditioner heating are also saved, and the service life of the cooling tower is prolonged. In addition, the heat exchangers are all made of stainless steel materials and can tolerate possible corrosion of trace oil and water vapor in exhaust of the air compressor.

The heat management system comprises an engine heat circulation loop flowing through an engine, a passenger cabin heat circulation loop flowing through a passenger cabin air outlet structure and a heat pump loop, and the heat pump loop exchanges heat with a first heat exchange flow path of the engine heat circulation loop. The temperature of engine cooling liquid is increased, the whole engine is heated, fuel oil is fully vaporized in the starting process of the engine, and lubricating oil is liquefied evenly. When a passenger cabin needs to be heated, the heat pump loop exchanges heat with the passenger cabin heat circulation loop through the inner cooler, and the engine heat circulation loop can exchange heat with the passenger cabin heat circulation loop through the second heat exchange flow path, so that waste heat generated when an engine works is reasonably utilized, and energy consumption of an automobile with the heat management system is reduced.

Provided are a solder alloy, a solder paste, a solder ball, and a solder joint which have a low melting point, are excellent in ductility, shear strength, and heat cycle resistance, further suppress the occurrence of open defects, and in addition, have reduced residual voids even at the time of joining in a large area. A solder alloy has an alloy composition of, by mass %, Bi: 35.0 to 68.0%, Sb: 0.1 to 2.0%, Ni: 0.010 to 0.050%, Ge: 0.007 to 0.090%, with the balance being Sn. Preferably, the alloy composition further contains, by mass %, at least one of Co, Ti, Al, Mn, As, Fe, Pd, Zn, Zr, Pb, In, Ce, P, and Ga: 0.1% or less in total. Further, this solder alloy can be suitably used for solder pastes, solder balls, and solder joints.

The utility model discloses a heat cyclic utilization type biomass steam boiler which comprises a base, a combustion chamber, a boiler body and a water tank, a scraper blade is movably connected in the combustion chamber, the upper end of the side, away from a feeding port, of the combustion chamber is connected with the water tank through a communicating pipe, and a connecting pipe is fixedly wound on the inner wall of the water tank. And one side of the top end of the water tank fixedly communicates with a second water inlet, an exhaust pipe communicating with the interior of the water tank is fixedly arranged on one side of the second water inlet, and an activated carbon filter screen plate is arranged in the exhaust pipe. The water heater has the advantages that smoke generated by combustion is conveyed into the connecting pipe through the communicating pipe and is coiled in the water tank through the connecting pipe, so that water in the water tank is heated by waste heat in the smoke, the heat utilization rate is improved, finally, the smoke is filtered and purified by the activated carbon filter screen plate and is exhausted from the exhaust pipe, and the environment is protected. And the situation that some unburnt impurities are doped in smoke to affect the environment is prevented.

This invention proposes a method and system for improving the power generation efficiency of steam turbines, relating to the field of gas-fired power generation technology in steel plants. The method includes: obtaining and purifying high-temperature flushing water from the blast furnace flushing process; using the purified high-temperature flushing water to heat a circulating medium; introducing the heated circulating medium into a thermal storage station to mitigate the intermittency and fluctuations of the waste heat from the flushing water; using the heated circulating medium from the thermal storage station to heat condensate; the cooled circulating medium after heat exchange entering a cold storage station; exchanging heat between the cooled circulating medium from the cold storage station and the purified high-temperature flushing water to form a closed-loop circulation of the circulating medium; and sending the heated condensate, after further multi-stage heating, into a boiler to generate steam to drive the steam turbine for power generation. The method and system proposed in this invention can effectively utilize the waste heat from the blast furnace flushing water, thereby improving overall efficiency.

The invention relates to a heating temperature control method and system of a solid heat storage device, and belongs to the field of temperature control. The water outlet temperature of the heat exchanger is used as a feedback value, the preset target water outlet temperature of the heat exchanger is used as a target value, the frequency of a fan used for forming airflow heat exchange circulation between the heat accumulator and the heat exchanger is calculated through the Dahlin algorithm, and then the amount of hot air fed into the heat exchanger after being heated by the heat accumulator is adjusted; the heat exchanger is used for supplying heat to heat consumers. The working frequency of the draught fan is calculated through the Dahlin algorithm, the air volume of hot air circulation between the heat accumulator and the heat exchanger can be effectively adjusted under the condition that overshoot is avoided, and then the water outlet temperature of the heat exchanger is controlled.

The invention provides a refrigerating system and an air conditioner, the refrigerating system comprises a first compressor, a first heat exchanger, a first valve, a second heat exchanger and an ejector, the first compressor, the first heat exchanger, the first valve and the second heat exchanger are connected to form at least partial structure of a first refrigerating loop; the ejector comprises a first inlet end, a second inlet end and a first outlet end, the first inlet end is communicated to the outlet end of the second heat exchanger, the second inlet end is communicated to the exhaust end of the first compressor, and the first outlet end of the ejector is communicated to the inlet end of the second heat exchanger. According to the invention, the evaporation or condensation heat exchange efficiency can be improved, so that a refrigerant which does not fully exchange heat can continuously participate in heat exchange circulation, and the compressor is prevented from sucking air and carrying liquid; the problem that in a heat exchanger of a refrigerating system in the prior art, heat exchange of refrigerants is not sufficient, and consequently the refrigerants are not completely evaporated or condensed is effectively solved.