温差冷凝制水供热、 空调、 发电系统 技术领域 Temperature difference condensing water heating, air conditioning, power generation system
本发明涉及一种制水、 供热、 空调、 发电系统, 特别是涉及一种利用低温制 冷机冷凝空气中水分制水、 供热、 空调、 发电的系统。 The present invention relates to a water-making, heating, air-conditioning, and power generation system, and in particular, to a water-making, heating, air-conditioning, and power generation system using water in a low-temperature refrigerator to condense air.
背景技术 Background technique
一直以来, 沙漠和高原等地区干旱缺水, 冷、 热无常, 更缺少电力, 用水都 是靠收集雨水和雪水或靠外来运进的水, 以上两种方法主要缺点是长时间储存雨 水和雪水, 将使水质变质; 外来运进的水, 经过长时间远距离的运输, 水质不好 并且成本高; 常年干旱造成的冷、 热无常和缺少电力, 给人类生存造成很大的困 难; 目前, 为汽轮发电机提供动力的装置仍是锅炉, 其 " 被加热工质" 是水, 水被加热汽化产生高压蒸汽驱动汽轮机发电。 它不仅要消耗大量的水, 更要消耗 大量的用于加热水的石油、 煤、 天然气等能源。 为开采、 运输和储存这些能源不 仅要耗费大量的人力和财力, 而且它们在燃烧后排出的废气和废渣又对环境造成 污染。 本人于 2000年 2月 24日申请的 "一种能源装置" 中的不足之处在于: 因 设多个气液交换器,使装置体积增大造价增加且由于降压缸设在气液交换器下端, 使液态低温工质很难在同一个压力状态下顺利回流至气液交换器内, 造成装置运 转困难, 另外 "一种能源装置"长期运转时, 冷能消耗无法补充。 For a long time, deserts and plateaus have suffered from drought and water shortage, cold and heat, and lack of electricity. Water is collected by collecting rainwater and snowwater or imported water. The main disadvantages of the above two methods are long-term storage of rainwater and Snow water will deteriorate the quality of the water; the incoming water, after long and long-distance transportation, the water quality is not good and the cost is high; the cold, heat, and lack of electricity caused by annual drought cause great difficulties for human survival; At present, the device that provides power to a turbo-generator is still a boiler, and its "heated working medium" is water, which is heated and vaporized to generate high-pressure steam to drive a steam turbine to generate electricity. It consumes not only a large amount of water, but also a large amount of energy such as oil, coal, and natural gas used to heat water. Not only does it take a lot of manpower and money to extract, transport, and store these energy sources, but the exhaust gases and waste residues they emit after combustion also pollute the environment. The shortcomings of the "One Energy Device" that I applied for on February 24, 2000 are: because of the installation of multiple gas-liquid exchangers, the device increases in size and cost, and because the pressure-reducing cylinder is located in the gas-liquid exchanger At the lower end, it is difficult for the liquid cryogenic working fluid to smoothly return to the gas-liquid exchanger under the same pressure state, which makes the operation of the device difficult. In addition, when a "energy device" is operated for a long time, the cold energy consumption cannot be supplemented.
发明内容 Summary of the Invention
鉴于以上事实, 本发明的目的是提供一种更科学合理方案来利用低温制冷机 联机在冷凝空气制水的同时供热、 空调、 发电的系统, 使沙漠和高原等干旱缺水, 冷、 热无常, 缺少电力的地区, 得到干净廉价的冷、 热水和冷、 热风及充足的电 力。 In view of the above facts, the object of the present invention is to provide a more scientific and reasonable solution to utilize a low-temperature refrigerator on-line system for heating, air conditioning, and power generation while condensing air to produce water, so that droughts such as deserts and plateaus lack water, cold, and heat. Impermanence, lack of power in the area, get clean and cheap cold, hot and cold, hot air and plenty of electricity.
本发明所提供的温差冷凝制水供热空调发电系统, 是由陶瓷隔热漆处理的气 液交换器和外壳用陶瓷隔热漆处理的等压位差注液器、 由耐低温的金属材料制成 的低温压力发生器、 由陶瓷隔热漆处理的气轮机、 由耐低温的金属材料制成的温 差冷凝制水器和外壳由隔热材料处理的空调冷气发生器、 储水罐、 风机、 由涡流 管制冷机用陶瓷隔热漆处理的蒸汽发生器由陶瓷隔热漆处理的蒸汽热水储罐、 风 机及外表由陶瓷隔热漆处理的管路、 外表用隔热材料处理的风管组成; 所述的温 差冷凝制水供热空调发电系统内, 还包括有低温压力发生装置、 冷能发电装置、 温差冷凝制水装置、 低温制氮制热装置;
所述的低温压力发生装置由陶瓷隔热漆处理的气液交换器和外壳用陶瓷隔热 漆处理的等压位差注液器及外表用陶瓷隔热漆处理的由电磁阀控制的管路组成, 气液交换器是用耐低温的金属材料如高锰低碳钢制成的中空球形壳体, 在气液交 换器的中空球形壳体上、 下中心各设一个通孔, 在气液交换器中空球形壳体上通 孔处的氮气出口通过管路与温差冷凝制水装置中的温差冷凝器 B组顶部的由电磁 阀控制的两个氮气入口及等压位差注液器顶部的由电磁阀控制的两个氮气入气口 相并连, 气液交换器下通孔处的入液口通过管路与等压位差注液器底部由电磁阀 控制的相连的液氮出口, 在气液交换器内还设有上下两端分别穿过壳体上下两部 与壳体通孔相连的螺旋换热盘管, 气液交换器内的螺旋换热盘管顶部的氮气入口 通过管路与气液交换器侧顶部的冷能发电装置的气轮机氮气出口及冷能发电装置 的等压位差注液器顶部由电磁阀控制的两个氮气入口相并连, 气液交换器内的螺 旋换热盘管下出口通过管路与气液交换器侧底部与冷能发电装置的等压位差注液 器顶部由电磁阀控制的液氮入口相连; The temperature difference condensing water heating and air-conditioning power generation system provided by the present invention is a gas-liquid exchanger treated with ceramic heat-insulating varnish, an isobaric liquid-filling injector treated with ceramic heat-insulating varnish on the shell, and a low-temperature-resistant metal material. Made of low temperature pressure generator, gas turbine treated with ceramic heat insulation paint, temperature difference condensing water generator made of low temperature resistant metal material and air conditioner cold air generator, water storage tank, fan made of heat insulation material Steam generators treated with ceramic heat-insulating paint for vortex tube refrigerators Steam hot water storage tanks treated with ceramic heat-insulating paint, fans and pipes treated with ceramic heat-insulating paint on the exterior, wind treated with heat-insulating materials on the exterior The temperature difference condensing water heating and air-conditioning power generation system further includes a low temperature pressure generating device, a cold energy power generating device, a temperature difference condensing water generating device, and a low temperature nitrogen heating device; The low-temperature pressure generating device includes a gas-liquid exchanger treated with ceramic heat-insulating varnish, a constant-pressure-diffusion injector treated with ceramic heat-insulating varnish for the shell, and a pipeline controlled by a solenoid valve treated with ceramic heat-insulating varnish on the exterior The gas-liquid exchanger is a hollow spherical shell made of a low-temperature-resistant metal material such as high-manganese low-carbon steel. A through hole is set in the upper and lower centers of the hollow spherical shell of the gas-liquid exchanger. The nitrogen outlet at the through hole on the hollow spherical shell of the exchanger passes through the pipeline and the two nitrogen inlets controlled by the solenoid valve at the top of the group B of the temperature difference condenser in the temperature difference condensation water production device and the top of the isobaric injector. The two nitrogen gas inlets controlled by the solenoid valve are connected in parallel. The liquid inlet at the lower hole of the gas-liquid exchanger is connected to the liquid nitrogen outlet controlled by the solenoid valve at the bottom of the isobaric injector through a pipeline. The gas-liquid exchanger is also provided with spiral heat exchange coils that pass through the upper and lower ends of the shell and are connected to the shell through holes. The nitrogen inlet at the top of the spiral heat exchanger coil in the gas-liquid exchanger passes through the pipeline. Cold energy power generation with gas-liquid exchanger side top The nitrogen outlet of the gas turbine installed and the two nitrogen inlets controlled by the solenoid valve on the top of the isobaric liquid injector of the cold power generation device are connected in parallel. The lower outlet of the spiral heat exchange coil in the gas-liquid exchanger is connected with the pipeline. The bottom of the gas-liquid exchanger side is connected to the liquid nitrogen inlet controlled by the solenoid valve on the top of the isobaric liquid injector of the cold power generation device;
其中所述的等压位差注液器是由两个是用耐低温的金属材料如高锰低碳钢制 成的中空柱形上、 下球顶的壳体组成, 在两个壳体上球顶各设三个通孔, 在两个 中空柱形壳体上部各设一个通孔, 在两个壳体下球顶各设一个通孔, 在两个壳体 上球顶各设一个与壳体通孔相连由电磁阀控制的排气阀, 在两个壳体球顶部各设 一个与壳体通孔相连的由电磁阀控制的与气液交换器顶部氮气出口及温差冷凝制 水装置的氮气入口相并连的入口, 在两个壳体球顶部还各设一个与壳体通孔相连 的与低温制氮制热装置末端的涡流管制冷机液氮出口相并连的液氮入口, 在两个 壳体球形底部各设一个与壳体通孔相连由电磁阀控制的与气液交换器底部的液氮 入口相并连的出口, 在两个中空柱形壳体中上部各设一个与壳体通孔相连的注液 阀口; The isobaric liquid injector is composed of two hollow cylindrical upper and lower domes made of low temperature resistant metal materials such as high manganese and low carbon steel. There are three through holes on the top of the ball, one through hole on the top of the two hollow cylindrical shells, one through hole on the bottom of the two shells, and one on the top of the two shells. The through hole of the shell is connected to an exhaust valve controlled by a solenoid valve. On the top of the two shell balls, there is a nitrogen outlet connected to the top of the gas-liquid exchanger and a temperature difference condensation water control device connected to the through hole of the shell and controlled by the solenoid valve. The two nitrogen inlets are connected in parallel. At the top of the two shell balls, a liquid nitrogen inlet connected to the liquid nitrogen outlet of the vortex tube refrigerator at the end of the low-temperature nitrogen heating device is also connected to the through holes of the casing. An outlet connected to the through hole of the casing and controlled by a solenoid valve and connected to the liquid nitrogen inlet at the bottom of the gas-liquid exchanger is connected to the spherical bottoms of the two casings. A liquid injection valve port connected to the through hole of the shell;
所述的冷能发电装置,由外壳用陶瓷隔热漆处理的等压位差注液器、由耐低温 的金属材料制成的在温差冷凝制水装置中交叉组合的 A组温差冷凝制水器和外壳 用陶瓷隔热漆处理的气轮机及外表用陶瓷隔热漆处理的管路组成; 所述的等压位 差注液器与低温压力发生装置所述的等压位差注液器结构相同, 在此不再详细说 明; 在等压位差注液器顶部各设一个与低温压力发生装置的气液交换器内的螺旋 换热盘管上入口和气轮机一端口的氮气出口相并连由电磁阀控制的入口, 在等压 位差注液器顶部还各设一个与低温压力发生装置的气液交换器内的螺旋换热盘管 下口液氮出口相连由电磁阀控制的液氮入口; 在等压位差注液器底部还各设一个
由电磁阀控制的液氮出口与在温差冷凝制水装置中交叉组合的 A组温差冷凝制水 器底部的液氮入口相连, 气轮机另一端口设有与在温差冷凝制水装置中交叉组合 的 A组温差冷凝制水器的氮气出口相连的氮气入口; The cold energy power generation device comprises a constant-pressure differential liquid injection device whose shell is treated with ceramic heat-insulating paint and a low-temperature-resistant metal material, which is a cross-group A temperature difference condensate water production device in a temperature difference condensate water production device. It is composed of a gas turbine treated with a ceramic heat-insulating paint on the casing and a pipeline treated with a ceramic heat-insulation paint on the exterior; the isobaric liquid injector and the isobaric liquid injector described in the low-temperature pressure generating device. The structure is the same and will not be described in detail here. Each top of the isobaric liquid injector is provided with a nitrogen heat outlet on the top of the spiral heat exchange coil in the gas-liquid exchanger of the low-temperature pressure generating device and the nitrogen outlet of the gas turbine. It is connected to the inlet controlled by the solenoid valve, and a liquid nitrogen outlet connected to the lower port of the spiral heat exchange coil in the gas-liquid exchanger of the low-temperature pressure generating device is connected to the liquid nitrogen outlet controlled by the solenoid valve. Nitrogen inlet; one at the bottom of the isobaric injector The liquid nitrogen outlet controlled by the solenoid valve is connected to the liquid nitrogen inlet at the bottom of the group A temperature difference condensing water generator which is cross-combined in the temperature difference condensing water making device. The other port of the gas turbine is provided with a cross combination in the temperature difference condensing water making device. The nitrogen inlet connected to the nitrogen outlet of the group A temperature difference condensing water generator;
所述的温差冷凝制水装置,由隔热材料处理的热风装置、交叉组合的由隔热材 料处理的 A、 B组温差冷凝制水器, 由隔热材料处理的连通风管、外表由隔热材料 处理的空调冷风发生器, 储水罐及外表由陶瓷隔热漆处理的管路和外表由隔热材 料处理的风管管路组成。 所述热风装置上开口由隔热材料处理的壳体内由上至下 设有: 风机, 蒸汽加热器及蒸汽入口、 电加热器、 磁力换向装置及两组送热风管 路; 其中壳体第一个下口与 A组的第一个温差冷凝制水器上口相连, 壳体中第二 个下口与 B组的第一个温差冷凝制水上口相连, 壳体中第三个的下口与 A组第二 个温差冷凝制水器上口相连, 壳体中第四个的的下口与 B组第二个温差冷凝制水 器上口相连, 蒸汽加热器的蒸汽入口与蒸汽热水储罐顶部的第五通孔上的蒸汽出 口相连。 所述的热风装置中的磁力换向装置是由中心相连设在上风管中的转向挡 板, 下设重力金属板两旁各设电磁线圈组成的电磁磁场。 1 所述交叉组合成的两 组温差冷凝制水器, A组两个温差冷凝制水器在冷能发电装置中配套; B组两个温 差冷凝制水器是设在风桶内的两个换热片式螺旋换热盘管, 在两个换热片式螺旋 换热盘管的上端是与两个由电磁阀控制的氮气入口相连, 下端与两个由电磁阀控 制的氮气出口; 所述由隔热材料处理的连通风管向上设有四个入口, 是的交叉的 将两个入口与冷能发电装置的两个风桶底部相连, 另外两个与温差冷凝制水装置 的两个风桶底部相连,在其侧面还经由电磁阀控制的冷风机与冷藏室风道管相连, 在其底部冷凝水出口处, 还由管路与空调冷风发生器顶部的入水管口相连; 所述 由隔热材料处理的空调冷风发生器是利用多管式进行气水交换, 在侧面带电磁阀 控制的通风机和空调送风管, 在气水交换器的顶部设两个管口, 是由上至下插入 气水交换器内底部的入口, 一个是与储水罐顶部的入水口相连的出水口; 所述的 储水罐是一个上设入水口, 侧设出水口的容器; The temperature difference condensing water-making device, a hot air device treated by a heat-insulating material, a cross-combined group A and B temperature difference condensing water-treatment device treated by a heat-insulating material, a connecting air pipe treated by a heat-insulating material, Air-conditioning cold wind generators with hot material treatment, water storage tanks and pipes with ceramic heat-resistant paint on the outside and air-pipe pipes with heat-resistant material on the outside. The upper opening of the hot-air device treated by a heat-insulating material is provided from top to bottom in the housing: a fan, a steam heater and a steam inlet, an electric heater, a magnetic reversing device, and two sets of hot-air pipelines; The first lower port is connected to the upper port of the first temperature difference condensing water generator in group A, the second lower port in the shell is connected to the first temperature difference condensing water upper group in group B, and the third The lower port is connected to the upper port of the second temperature difference condensing water generator in group A, the lower port of the fourth in the casing is connected to the upper port of the second temperature difference condensing water generator in group B, and the steam inlet of the steam heater is connected to the steam The steam outlet on the fifth through hole on the top of the hot water storage tank is connected. The magnetic reversing device in the hot air device is an electromagnetic magnetic field composed of a steering baffle provided in the upper air pipe connected to the center, and a gravity metal plate provided with electromagnetic coils on both sides. 1 The two groups of temperature difference condensing water generators combined as described above, two temperature difference condensing water generators in group A are matched in a cold energy power generation device; the two temperature difference condensing water generators in group B are two in the air bucket. The heat exchange fin spiral heat exchange coils are connected at the upper end of the two heat exchange fin spiral heat exchange coils with two nitrogen inlets controlled by solenoid valves, and the lower end is connected with two nitrogen outlets controlled by solenoid valves; The above-mentioned connecting ducts treated by heat-insulating materials are provided with four inlets upwards, and the two inlets are connected to the bottom of two air buckets of the cold power generating device, and the other two are connected to two of the temperature difference condensing water generating device. The bottom of the air bucket is connected, and a cold air fan controlled by a solenoid valve is connected to the air duct pipe of the refrigerating compartment on the side thereof. At the bottom of the condensate water outlet, a pipe is also connected to the water inlet pipe top of the air conditioning cold wind generator; The air-conditioning cold wind generator treated by heat-insulating material uses multi-tube type for air-water exchange. The fan and air-conditioning air supply pipe are controlled by solenoid valves on the side. Two nozzles are set on the top of the air-water exchanger. Insert from top to bottom The water inlet of the bottom of the exchanger, a water outlet and a water storage tank inlet connected to the top; said water storage tank is provided on a water inlet, an outlet side disposed vessel;
所述的低温制氮制热装置:由三台涡流管式制冷机组成的涡流管式制冷机组、 和由三台蒸汽发生器组成的蒸汽发生器组, 蒸汽热水储罐及外表由陶瓷隔热漆处 理的管路组成。 所述的涡流管式冷机组是由三台涡流管式制冷机首尾串连相接组 成的; 外表由隔热材料处理的顶部带自动冷风排放阀的蒸汽发生器是由金属材料 制成的套在三台涡流管式制冷机后面散热管上的中空式柱型上、 下球顶处各设一 个通孔的, 外表由隔热材料处理的蒸汽热水储罐是由金属材料制成内设叁组螺旋
换热盘管的中空式上下球顶的柱型圆桶, 在蒸汽热水储罐上部球顶设五个通孔, 在蒸汽热水储罐中上部设两个通孔, 在蒸汽热水储罐中部设一个通孔, 在蒸汽热 水储罐底部设四个通孔。 第一台涡流管式冷机的氮气入口与温差冷凝制水装置的The low-temperature nitrogen and heating device: a vortex tube refrigeration unit composed of three vortex tube refrigerators, and a steam generator group composed of three steam generators, and a steam hot water storage tank and a ceramic partition Composition of hot-painted pipes. The vortex tube cold unit is composed of three vortex tube refrigerators connected in series end to end. The steam generator with an automatic cold air discharge valve on the top treated by heat insulation material is a jacket made of metal material. A through-hole is provided on the hollow cylindrical upper and lower ball tops of the heat dissipation tubes behind the three vortex tube refrigerators, and the steam and hot water storage tanks treated by heat-insulating materials on the outside are made of metal materials and built-in Three sets of spirals Hollow upper and lower dome-shaped cylindrical barrels of heat exchange coils are provided with five through holes in the upper part of the steam hot water storage tank, and two through holes in the upper part of the steam hot water storage tank. One through hole is set in the middle of the tank, and four through holes are set in the bottom of the steam hot water storage tank. The nitrogen inlet of the first vortex tube chiller and the temperature difference
B 组温差冷凝制水器的底部设有两个的氮气出口相并连, 第一台涡流管式制冷机 的氮气出口与第二台涡流管式制冷机的氮气入口相连, 第二台涡流管式制冷机的 氮气出口与第三台涡流管式制冷机的氮气入口相连, 第三台涡流管式制冷机的液 氮出口与低温压力发生装置的等压位差注液器顶部的液氮入口相并连。 套在三台 涡流管制制冷机上的蒸汽发生器上球顶通孔处, 各设一个经蒸汽热水储罐上球顶 部三个通孔与蒸汽热水储罐内的叁个螺旋换热盘管上的蒸汽入口单独相连的蒸汽 出口; 三个蒸汽发生器下球顶的通孔处, 的三个冷凝水入口与蒸汽热水储罐下球 顶通孔内的螺旋换热盘管的冷凝水出口和注水阀门相并连, 在蒸汽热水储罐球顶 另外两个通孔处设两个由电磁阀控制的蒸汽出口, 在蒸汽热水储罐球顶另一个通 孔处设一个由电脑控制的水位控制仪, 在蒸汽热水储罐中上部通孔处设一个由电 磁阀控制的开水出口, 在蒸汽热水储罐中部通孔处设一个由电磁阀控制的热水出 口, 在蒸汽热水储罐底部另一个通孔处设一个由电磁阀控制的自来水入口。 There are two nitrogen outlets connected in parallel at the bottom of the group B temperature difference condensing water generator. The nitrogen outlet of the first vortex tube refrigerator is connected to the nitrogen inlet of the second vortex tube refrigerator. The second vortex tube The nitrogen outlet of the refrigerator is connected to the nitrogen inlet of the third vortex tube refrigerator. The liquid nitrogen outlet of the third vortex tube refrigerator is connected to the liquid nitrogen inlet on the top of the isobaric liquid injector of the low-temperature pressure generator. Connected. Three through-holes on the top of the ball of the steam hot water storage tank and three spiral heat exchange coils in the steam and hot water storage tank are set on the ball top through holes of the steam generator on the three vortex control refrigerators. The steam inlet on the upper side is separately connected to the steam outlet; the three condensate water inlets at the lower hole of the dome of the three steam generators and the condensate water in the spiral heat exchange coil in the lower hole of the dome of the steam hot water storage tank The outlet and the water injection valve are connected in parallel. Two steam outlets controlled by the solenoid valve are provided at the other two through holes of the dome of the steam hot water storage tank, and a computer is installed at the other through hole of the dome of the steam hot water storage tank. The controlled water level controller is provided with a boiling water outlet controlled by a solenoid valve at the upper through hole in the steam hot water storage tank, and a hot water outlet controlled by a solenoid valve at the through hole in the middle of the steam hot water storage tank. At the other through hole at the bottom of the hot water storage tank, there is a tap water inlet controlled by a solenoid valve.
本发明主要包括有: 低温压力发生装置、冷能发电装置、温差冷凝制水装置、 低温制氮制热装置; 所述的温差冷凝制水、 供热、 空调、 发电系统内, 还包括有 低温压力发生器、 气轮机、 等压位差注液器、 A、 B两组共四个温差冷凝制水器、 空调冷风发生器、 储水罐、 风机、 三台涡流管式制冷机、 三个蒸汽发生器、 蒸汽 热水储罐、 及管路构成; The invention mainly includes: a low-temperature pressure generating device, a cold energy power generation device, a temperature difference condensing water-making device, and a low-temperature nitrogen heating device; the temperature difference condensing water-making, heating, air-conditioning, and power generation system also includes low temperature Pressure generators, gas turbines, isobaric liquid injectors, A, B two groups of four temperature difference condensing water generators, air conditioning cold air generators, water storage tanks, fans, three vortex tube refrigerators, three A steam generator, a steam hot water storage tank, and a pipeline;
所述的低温压力发生装置最好由陶瓷隔热漆处理的气液交换器和外壳最好用 陶瓷隔热漆处理的等压位差注液器及外表最好用陶瓷隔热漆处理的由电磁阀控制 的管路组成, 气液交换器最好是用耐低温的金属材料如高锰低碳钢制成的中空球 形壳体, 在气液交换器的中空球形壳体上、 下中心各设一个通孔, 在气液交换器 中空球形壳体上通孔处的氮气出口通过管路与温差冷凝制水装置中的温差冷凝器 B 组顶部的由电磁阀控制的两个氮气入口及等压位差注液器顶部的由电磁阀控制 的两个氮气入气口相并连, 气液交换器下通孔处的入液口通过管路与等压位差注 液器底部由电磁阀控制的相连的液氮出口, 在气液交换器内还设有上下两端分别 穿过壳体上下两部与壳体通孔相连的螺旋换热盘管, 气液交换器内的螺旋换热盘 管顶部的氮气入口通过管路与气液交换器侧顶部的冷能发电装置的气轮机氮气出 口及冷能发电装置的等压位差注液器顶部由电磁阀控制的两个氮气入口相并连,
气液交换器内的螺旋换热盘管下出口通过管路与气液交换器侧底部与冷能发电装 置的等压位差注液器顶部由电磁阀控制的液氮入口相连; The low-temperature pressure generating device is preferably a gas-liquid exchanger treated with ceramic heat-insulating varnish and an isobaric liquid injector with a ceramic heat-insulating varnish and an outer surface preferably made of ceramic heat-insulating varnish. The solenoid valve controls the pipeline composition. The gas-liquid exchanger is preferably a hollow spherical shell made of a low temperature resistant metal material such as high manganese and low carbon steel. The upper and lower centers of the hollow spherical shell of the gas-liquid exchanger are each A through hole is provided, and the nitrogen outlet at the through hole on the hollow spherical shell of the gas-liquid exchanger is passed through a pipeline and the temperature difference condenser B in the temperature difference condensation water making device. The two nitrogen inlets controlled by the solenoid valve and the like The two nitrogen gas inlets controlled by the solenoid valve on the top of the pressure difference injector are connected in parallel. The liquid inlet at the lower hole of the gas-liquid exchanger is controlled by a solenoid valve through the pipeline and the bottom of the equal pressure injector. The connected liquid nitrogen outlets are also provided in the gas-liquid exchanger with spiral heat exchange coils that pass through the upper and lower ends of the casing and the two through holes of the casing, and the spiral heat exchanger discs in the gas-liquid exchanger. The nitrogen inlet at the top of the tube is connected to the gas-liquid exchanger through the pipeline Injection pressure head of the liquid and other gas turbine cooling nitrogen outlet power generating device and a cold top of the top two power generating device controlled by the nitrogen inlet and connected with the solenoid valve, The lower outlet of the spiral heat exchange coil in the gas-liquid exchanger is connected with the liquid nitrogen inlet controlled by the solenoid valve at the top of the isobaric injector of the cold-energy power generator through the bottom of the side of the gas-liquid exchanger;
其中所述的等压位差注液器最好是由两个是用耐低温的金属材料如高锰低碳 钢制成的中空柱形上下设球顶的壳体组成, 在两个壳体上球顶各设三个通孔, 在 两个中空形壳体中上部最好各设一个通孔, 在两个壳体下球顶各设一个通孔, 在 两个壳体上球顶各设一个与壳体通孔相连由电磁阀控制的排气阔, 在两个壳体球 顶部各设一个与壳体通孔相连的由电磁阀控制的与气液交换器顶部氮气出口及温 差冷凝制水装置的氮气入口相并连的入口, 在两个壳体球顶部还各设一个与壳体 通孔相连的与低温制氮制热装置末端的涡流管制冷机液氮出口相并连的液氮入 口, 在两个壳体球形底部设一个与壳体通孔相连由电磁阀控制的与气液交换器底 部的液氮入口相并连的出口, 在两个中空桶形壳体中上部各设一个与壳体通孔相 连的注液阀口; The isobaric liquid injection device mentioned above is preferably composed of two hollow cylindrical shells with a dome top and bottom made of a low temperature resistant metal material such as high manganese and low carbon steel. There are three through holes on the top of the ball, one through hole in the middle and upper part of the two hollow shells, one through hole on the bottom of the two shells, and one on the two shells. An exhaust valve controlled by a solenoid valve is connected to the through hole of the shell, and a nitrogen outlet and a temperature difference condensation at the top of the gas-liquid exchanger controlled by a solenoid valve are connected to the top of the two shell balls. The nitrogen inlets of the water-making device are connected in parallel. At the top of the two shell balls, there is also a hole connected to the through hole of the shell and connected to the liquid nitrogen outlet of the vortex tube refrigerator at the end of the low-temperature nitrogen heating device. Liquid nitrogen inlet, an outlet connected to the through hole of the casing and controlled by a solenoid valve and connected to the liquid nitrogen inlet at the bottom of the gas-liquid exchanger is connected to the spherical bottom of the two shells, and the upper and middle parts of the two hollow barrel-shaped shells Each is provided with a liquid injection valve port connected to the through hole of the shell;
所述的冷能发电装置, 最好由外壳由陶瓷隔热漆处理的等压位差注液器、 由 耐低温的金属材料制成的在湿差冷凝制水装置中交叉组合的 A组温差冷凝制水器 和外壳由陶瓷隔热漆处理的气轮机及外表由陶瓷隔热漆处理的管路组成, 所述的 等压位差注液器与低温压力发生装置所述的等压位差注液器结构相同, 在此不再 详细说明。 在等压位差注液器顶部各设一个与低温压力发生装置的气液交换器内 的螺旋换热盘管上入口和气轮机一端口的氮气出口相并连由电磁阀控制的入口, 在等压位差注液器顶部还各设一个与低温压力发生装置的气液交换器内的螺旋换 热盘管下口液氮出口相连由电磁阔控制的液氮入口, 在等压位差注液器底部还各 设一个由电磁阀控制的液氮出口与在温差冷凝制水装置中交叉组合的 A组温差冷 凝制水器底部的液氮入口相连, 气轮机另一端口最好设有与在温差冷凝制水装置 中交叉组合的 A组温差冷凝制水器的氮气出口相连的氮气入口; The cold energy power generation device is preferably a group A temperature difference that is cross-combined in a wet differential condensing water device made of a low-temperature-resistant metal material, an isobaric liquid injector with a shell made of ceramic insulation paint, and a shell made of ceramic insulation paint. The condensing water generator and the shell are made of a ceramic heat-treated paint-treated gas turbine and the pipeline is made of ceramic heat-treated paint, and the isobaric pressure difference injector and the isobaric pressure difference described in the low-temperature pressure generator The structure of the injector is the same and will not be described in detail here. On the top of the isobaric injector, an inlet connected to a solenoid valve controlled by an inlet of a spiral heat exchange coil in a gas-liquid exchanger of a low-temperature pressure generating device and a nitrogen outlet of a port of the gas turbine is provided. At the top of the pressure difference injector, there is a liquid nitrogen inlet connected to the lower end of the spiral heat exchange coil in the gas-liquid exchanger of the low-temperature pressure generating device. A liquid nitrogen outlet controlled by a solenoid valve is also provided at the bottom of the device, which is connected to the liquid nitrogen inlet at the bottom of the group A temperature difference condensing water generator which is cross-combined in the temperature difference condensing water device. The other port of the gas turbine is preferably provided with The nitrogen inlet connected to the nitrogen outlet of the group A temperature difference condensing water generator in the cross combination in the temperature difference condensing water device;
所述的温差冷凝制水装置, 最好由隔热材料处理的热风装置、 交叉组合的由 隔热材料处理的八、 B组温差冷凝制水器, 由隔热材料处理的连通风管、 外表由隔 热材料处理的空调冷风发生器, 储水罐及外表由陶瓷隔热漆处理的管路和外表由 隔热材料处理的风管管路组成; 所述热风装置上开口的由隔热材料处理的壳体内 由上至下设有: 风机, 蒸汽加热器及蒸汽入口, 电加热器、 磁力换向装置及两组 送热风管路: 其中壳体第一个下口与 A组的第一个温差冷凝制水器上口相连, 壳 体中第二个下口与 B组的第一个温差冷凝制水上口相连, 壳体中第三个的下口与 A组第二个温差冷凝制水器上口相连, 壳体中第四个的的下口与 B组第二个温差
冷凝制水器上口相连, 蒸汽加热器的蒸汽入口与蒸汽热水储罐顶部的第五通孔上 的蒸汽出口相连; 所述的热风装置中的磁力换向装置最好是由中心相连设在上风 管中的转向挡板, 下设重力金属板, 两旁各设电磁线圈所组成的电磁磁场; 所述 交叉组合成的两组温差冷凝制水器, A组两个温差冷凝制水器在冷能发电装置中 配套; B 组两个温差冷凝制水器是设在风桶内的两个换热片式螺旋换热盘管, 在 两个换热片式螺旋换热盘管的上端最好是与两个由电磁阀控制的氮气入口相连, 下端最好是与两个由电磁阀控制的氮气出口; 所述由隔热材料处理的连通风管向 上最好设有四个入口, 最好是的交叉的将两个入口与冷能发电装置的两个风桶底 部相连, 另外两个与温差冷凝制水装置的两个风桶底部相连, 在其侧面还经由电 磁阀控制的冷风机与冷藏室风道管相连, 在其底部冷凝水出口处, 由管路与空调 冷风发生器顶部的入水管口相连; 所述由隔热材料处理的空调冷风发生器是利用 多管式进行气水交换, 在侧面由电磁阀控制的通风机和空调送风管, 在气水交换 器的顶部设两个管口, 一是由上至下插入气水交换器内底部的入口, 另一个是与 储水罐顶部的入水口相连的出水口; 所述的储水罐是一个上设入水口, 侧设出水 口的容器; The temperature difference condensing water generating device is preferably a hot air device processed by a thermal insulation material, a cross combination of eight or B group temperature difference condensing water generators, a connecting air pipe processed by a thermal insulation material, an exterior The air-conditioning cold wind generator treated with heat-insulating material, the water storage tank and the pipe whose outer surface is treated with ceramic heat-insulating paint and the outer-pipe treated by heat-insulating material; the opening of the hot-air device is made of heat-insulating material. From the top of the processed shell, there are: fans, steam heaters and steam inlets, electric heaters, magnetic reversing devices, and two sets of hot air ducts: the first lower port of the shell and the first The upper port of a temperature difference condensing water generator is connected, the second lower port in the housing is connected to the first temperature difference condensing water generator in group B, and the third lower port in the housing is condensed with the second temperature difference in group A The upper mouth of the water purifier is connected, and the lower mouth of the fourth in the shell is different from the second temperature difference in group B. The upper port of the condensing water generator is connected, the steam inlet of the steam heater is connected to the steam outlet on the fifth through hole on the top of the steam hot water storage tank; the magnetic commutation device in the hot air device is preferably connected by the center. The steering baffle in the upwind pipe is provided with a gravity metal plate below, and an electromagnetic magnetic field composed of electromagnetic coils is arranged on each side; the two groups of temperature difference condensation water heaters formed by the cross combination, and the group of two temperature difference condensation water heaters in group A It is matched in the cold energy power generation device; the two temperature difference condensing water generators in group B are two heat exchange fin spiral heat exchange coils located in the air bucket, at the upper ends of the two heat exchange fin spiral heat exchange coils. Preferably, it is connected to two nitrogen inlets controlled by a solenoid valve, and the lower end is preferably connected to two nitrogen outlets controlled by a solenoid valve; preferably, the communication duct processed by the heat insulation material is provided with four inlets upward, It is better to connect the two inlets to the bottom of the two air buckets of the cold energy power generation device, and the other two to the bottom of the two air buckets of the temperature difference condensing water production device, and the cold air controlled by the solenoid valve on its side Machine and refrigerator air duct It is connected to the condensate water outlet at the bottom by a pipe connected to the water inlet on the top of the air-conditioning cold wind generator. The air-conditioning cold wind generator treated with heat-insulating material uses multi-tube type for gas-water exchange. The ventilator and air-conditioning air supply pipe controlled by the solenoid valve are provided with two nozzles on the top of the air-water exchanger, one is inserted from the bottom to the inlet of the inner part of the air-water exchanger, and the other is connected with the top of the water storage tank. A water outlet connected to a water inlet; the water storage tank is a container provided with a water inlet on the side and a water outlet on the side;
所述的低温制氮制热装置: 最好由三台涡流管式制冷机组成的涡流管制冷机 组、 和由三台蒸汽发生器组成的蒸汽发生器组, 蒸汽热水储罐及外表由陶瓷隔热 漆处理的管路组成; 所述的涡流管制冷机组最好是由三台涡流管式制冷机首尾串 连相接组成的; 外表由隔热材料处理的顶部带自动冷风排放阀的蒸汽发生器是由 金属材料制成的套在三台涡流管制冷机后面散热管上的中空式柱型上下球顶处各 设一个通孔的; 最好外表由隔热材料处理的蒸汽热水储罐是由金属材料制成内设 叁组螺旋换热盘管的中空式上下球顶的柱型圆桶, 在蒸汽热水储罐上部球顶设五 个通孔, 在蒸汽热水储罐中上部设两个通孔, 在蒸汽热水储罐中部设一个通孔, 在蒸汽热水储罐底部设四个通孔。 第一台涡流管式制冷机的氮气入口与温差冷凝 制水装置的 B组温差冷凝制水器的底部设有两个的氮气出口相并连, 第一台涡流 管式制冷机的氮气出口与第二台涡流管式制冷机的氮气入口相连, 第二台涡流管 式制冷机的氮气出口与第三台涡流管式冷机的氮气入口相连, 第三台涡流管式制 冷机的液氮出口与低温压力发生装置的等压位差注液器顶部的液氮入口相并连。 套在三台涡流管式制冷机上的三个蒸汽发生器上球顶通孔各设一个经蒸汽热水储 罐上球顶部三个通孔与蒸汽热水储罐内的叁个螺旋换热盘管上的蒸汽入口单独相 连的蒸汽出口, 三个蒸汽发生器下球顶通孔处, 各设有的冷凝水入口与蒸汽热水
储罐下球顶通孔内的三个螺旋换热盘管的冷凝水出口及注水阀门相并连, 在蒸汽 热水储罐球顶另外两个通孔处设两个由电磁阀控制的蒸汽出口, 在蒸汽热水储罐 球顶另一个通孔处设一个由电脑控制的水位控制仪, 在蒸汽热水储罐中上部通孔 处设一个由电磁阀控制的开水出口, 在蒸汽热水储罐中部通孔处设一个由电磁阀 控制的热水出口, 在蒸汽热水储罐底部另一个通孔处设一个由电磁阀控制的自来 水入口。 The low-temperature nitrogen and heating device: a vortex tube refrigeration unit preferably composed of three vortex tube refrigerators, and a steam generator group composed of three steam generators, and a steam and hot water storage tank and a ceramic surface It is composed of pipelines treated with heat-insulating paint; the vortex tube refrigeration unit is preferably composed of three vortex-tube refrigerators connected in series end to end; the exterior is treated with heat insulation material and the top is equipped with an automatic cold air discharge valve. The generator is made of metal material and is provided with a through hole at the hollow cylindrical upper and lower dome on the heat dissipation tube behind the three vortex tube refrigerators; the outer surface of the steam and hot water treated with thermal insulation material is preferred The tank is a cylindrical barrel made of metal material with three sets of spiral heat exchange coils. It has five through holes on the top of the steam hot water storage tank. There are two through holes in the upper part, one through hole in the middle of the steam hot water storage tank, and four through holes in the bottom of the steam hot water storage tank. The nitrogen inlet of the first vortex tube refrigerator is connected in parallel with two nitrogen outlets at the bottom of the group B temperature difference condensing water generator of the temperature difference condensing water device. The nitrogen outlet of the first vortex tube refrigerator is connected with The nitrogen inlet of the second vortex tube refrigerator is connected, the nitrogen outlet of the second vortex tube refrigerator is connected to the nitrogen inlet of the third vortex tube refrigerator, and the liquid nitrogen outlet of the third vortex tube refrigerator. It is connected in parallel with the liquid nitrogen inlet on the top of the isobaric liquid injector of the low-temperature pressure generating device. Three through holes on the top of the ball of the three steam generators installed on three vortex tube refrigerators are provided with three through holes on the top of the ball through the hot water tank and three spiral heat exchange plates in the hot water tank The steam inlet on the tube is connected to the steam outlet separately. At the through hole of the dome under the three steam generators, each has a condensate inlet and steam hot water. The condensed water outlets of the three spiral heat exchange coils and the water injection valve in the through hole of the ball top of the storage tank are connected in parallel, and two steam holes controlled by the solenoid valve are provided at the other two through holes of the ball top of the steam hot water storage tank. At the outlet, a water level controller controlled by a computer is set at another through hole in the dome of the steam hot water storage tank, and a boiling water outlet controlled by a solenoid valve is set at the upper through hole in the steam hot water storage tank. A hot water outlet controlled by a solenoid valve is set at a through hole in the middle of the storage tank, and a tap water inlet controlled by a solenoid valve is set at another through hole at the bottom of the steam hot water storage tank.
本发明比现有技术有相比具有如下优点: 一次性启动, 运转时无能耗的冷凝 制水并提供热水、 热风、 冷风、 蒸汽和电力。 Compared with the prior art, the present invention has the following advantages: one-time start, condensed water without energy consumption during operation, and provides hot water, hot air, cold air, steam and electricity.
现在结合附图对本发明的实施例做详细说明, 以使对本发明有更清晰更详细 的了解。 The embodiments of the present invention will now be described in detail with reference to the drawings, so as to have a clearer and more detailed understanding of the present invention.
附图说明 BRIEF DESCRIPTION OF THE DRAWINGS
图 1为本发明温差冷凝制水、 供热、 空调、 发电系统的实施示意图。 FIG. 1 is a schematic diagram of the implementation of the temperature difference condensation water production, heating, air conditioning, and power generation system of the present invention.
具体实施方式 detailed description
本发明提供的温差冷凝制水、 供热、 空调、 发电系统, 由低温压力发生装置、 冷能发电装置、 温差冷凝制水装置以及低温制氮制热装置相互连接而成: The temperature difference condensation water production, heating, air conditioning, and power generation system provided by the present invention is formed by interconnecting a low temperature pressure generating device, a cold energy power generation device, a temperature difference condensation water production device, and a low temperature nitrogen heating device.
所述的低温压力发生装置由气液交换器 16和两个等压位差注液器 1、 10及由 电磁阀控制的管路组成: The low-temperature pressure generating device is composed of a gas-liquid exchanger 16 and two equal-pressure-diffusion injectors 1, 10, and a pipeline controlled by a solenoid valve:
其中所述气液交换器 16, 是在中空球形壳体上下各设一个通孔, 上通孔为气 液交换器 16的氮气出口 13,下通孔为气液交换器 16的液氮入口 18,气液交换器 16内还设有上下两端分别穿过壳体上下两部与壳体通孔相连的螺旋换热盘管 15, 螺旋换热盘管 15设有上入口 14和下出口 17; The gas-liquid exchanger 16 is provided with a through hole on the upper and lower sides of the hollow spherical shell. The upper through-hole is the nitrogen outlet 13 of the gas-liquid exchanger 16 and the lower through-hole is the liquid nitrogen inlet 18 of the gas-liquid exchanger 16. The gas-liquid exchanger 16 is also provided with a spiral heat exchanger coil 15 connected to the shell through hole at the upper and lower ends of the upper and lower ends respectively. The spiral heat exchanger coil 15 is provided with an upper inlet 14 and a lower outlet 17 ;
其中所述的两个等压位差注液器 1、 10在壳体中上部各设三个与壳体相连通 的管孔, 其一通孔为由电磁阀控制的排气口 5、 9, 另一通孔为由电磁阔控制的氮 气入口 4、 8, 第三个通孔为由电磁阀控制的液氮入口 3、 6, 在壳体中上部各设一 个与壳体相连通的注液阀口 2、 7; 在壳体底部各设一个由电磁阀控制的与壳体相 连通的出液口, 11、 12; The two isobaric liquid injectors 1 and 10 described above are provided with three pipe holes connected to the housing in the upper and middle parts of the housing. One of the through holes is an exhaust port 5, 9 controlled by a solenoid valve. The other through hole is the nitrogen inlets 4 and 8 controlled by the solenoid, the third through hole is the liquid nitrogen inlets 3 and 6 controlled by the solenoid valve, and a liquid injection valve connected to the housing is provided in the upper part of the housing. Ports 2 and 7; a liquid outlet which is controlled by a solenoid valve and communicates with the casing is provided at the bottom of the casing, 11 and 12;
所述的冷能发电装置,由两个等压位差注液器 30、 29和在温差冷凝制水装置 中交叉组合的 A组温差冷凝制水器 52、 59和一个气轮机 28及管路组成 : The cold energy power generation device comprises two equal pressure differential liquid injection devices 30 and 29 and a group A temperature difference condensing water generator 52, 59 and a gas turbine 28 and pipelines which are combined in a temperature difference condensing water device. Composition:
其中所述等压位差注液器 30、 29在壳体中上部各设三个与壳体相连通的管 孔, 其一通孔为由电磁阀控制的排气口 21、 25, 另一通孔为由电磁阀控制的氮气 入口 20、 24, 第三个通孔为由电磁阀控制的液氮入口 19、 22, 在壳体中上部各设
一个与壳体相连通的注液阀口 23、 26; 在壳体底部各设一个由电磁阀控制的与壳 体相连通的出液口, 31、 32; Wherein, the isobaric liquid injectors 30 and 29 are provided with three pipe holes in the upper and middle parts of the housing, which communicate with the housing. One of the through holes is an exhaust port 21, 25 controlled by a solenoid valve, and the other is a through hole. The nitrogen inlets 20 and 24 are controlled by solenoid valves. The third through hole is the liquid nitrogen inlets 19 and 22 controlled by solenoid valves. A liquid injection valve port 23, 26 connected to the housing; a liquid outlet port 31, 32 controlled by a solenoid valve and connected to the housing is provided at the bottom of the housing;
其中所述的交叉组合的 A温差冷凝制水器 52、 59中还包括有,设在 A组温差 冷凝制水器 52、 59的风桶 51、 60内的两个换热片式螺旋换热盘管 50、 58, 在这 两个换热片式螺旋换热盘管 50、 58顶部各设一个氮气出口 49、 57, 并在底部各 设一个液氮入口 66、 68; The cross-combined A temperature difference condensing water generators 52 and 59 also include two heat exchange fin spiral heat exchangers provided in the air barrels 51 and 60 of the group A temperature difference condensing water generators 52 and 59. Coil tubes 50, 58. A nitrogen outlet 49, 57 is provided at the top of each of the two heat exchange plate spiral heat exchange coils 50, 58, and a liquid nitrogen inlet 66, 68 is provided at the bottom.
其中所述的气轮机 28是一端设氮气出口 27—端设氮气入口 33的蜗牛式密 封、 保温、 保压的能带动发电机做功的装置; The gas turbine 28 is a snail-type seal, heat preservation and pressure holding device with a nitrogen outlet 27 at one end and a nitrogen inlet 33 at the end, which can drive the generator to perform work;
所述的温差冷凝制水装置,由热风装置 35和交叉组合的 A、B组温差冷凝制水 器, 连通风管 72、 空调冷风发生器 76和储水罐 80及管路组成: The temperature difference condensing water-making device is composed of a hot air device 35 and a cross-combined group A and B temperature difference condensing water device, a connecting air pipe 72, an air-conditioning cold wind generator 76, a water storage tank 80, and a pipeline:
其中所述热风装置 35上开口的壳体 40内由上至下设有: 风机 34, 蒸汽加热 器 37及蒸汽入口 36, 电加热器 38、磁力换向装置 41及两组送热风管路: 45、 46、 47、 48, 其中 45的下口与 A组 52的上口相连, 46的下口与 B组 53的上口相连, 47的下口与 A组 59的上口相连, 48的下口与 B组 63的上口相连, 蒸汽加热器 37的蒸汽入口 36与蒸汽热水储罐 115顶部的第五通孔上的蒸汽出口 98相连; 其中热风装置 35中的磁力换向装置 41是与中轴相连、 上设风向挡板 39, 下 设重力金属板 42、 两旁各设电磁线圈的电磁磁场 44、 42的装置; The hot air device 35 is provided with a shell 40 opened from top to bottom: a fan 34, a steam heater 37 and a steam inlet 36, an electric heater 38, a magnetic reversing device 41, and two sets of hot air pipelines. : 45, 46, 47, 48, of which the lower port of 45 is connected to the upper port of group A 52, the lower port of 46 is connected to the upper port of group B 53, the lower port of 47 is connected to the upper port of group A 59, 48 The lower port is connected to the upper port of group B 63, and the steam inlet 36 of the steam heater 37 is connected to the steam outlet 98 on the fifth through hole on the top of the steam hot water storage tank 115; wherein the magnetic reversing device in the hot air device 35 41 is a device connected to the central axis, provided with a wind direction baffle 39 on the upper side, a gravity metal plate 42 on the lower side, and electromagnetic magnetic fields 44, 42 on both sides with electromagnetic coils;
其中所述交叉组合成的两组温差冷凝制水器, A组 52、 59, 在冷能发电装置 中配套; B组 53、 63, 由设在风桶 56、 64内的换热片式螺旋换热盘管 54、 62, 该换热片式螺旋换热盘管 54、 62的上端是由电磁阀控制的氮气入口 55、 61相连, 下端是由电磁阀控制的氮气出口 67、 69; The two groups of cross-condensation condensate water generators mentioned above, A group 52, 59, are matched in the cold energy power generation device; Group B 53, 63, are composed of heat exchange plate spirals arranged in the air buckets 56, 64 Heat exchange coils 54, 62. The upper ends of the heat exchange fin spiral heat exchange coils 54, 62 are connected by nitrogen inlets 55, 61 controlled by solenoid valves, and the lower ends are nitrogen outlets 67, 69 controlled by solenoid valves.
其中所述的连通风管 64向上设有四个入口,其中的交叉的两个入口与冷能发 电装置的风桶 51、 60底部相连, 另外两个与温差冷凝制水装置的两个风桶 56、 6 底部相连, 在其侧面还经由电磁阀控制的冷风机 71与冷藏室风道管 70相连, 在其底部冷凝水出口处,还由管路与空调冷风发生器 76顶部的入水管口 75相连; 其中所述的空调冷风发生器 76是利用多管式进行气水交换,在侧面带电磁阀 控制的通风机 74和空调送风管 73, 在气水交换器的顶部设两个管口, 一个是由 上至下插入气水交换器内底部的入口 75,一个是与储水罐 80顶部的入水口 78相 连的出水口 77; The above-mentioned connecting air duct 64 is provided with four inlets upwards, two of which are intersected with the bottoms of the air buckets 51 and 60 of the cold energy power generating device, and the other two are connected with the two air buckets of the temperature difference condensing water making device. 56 and 6 are connected at the bottom, and on the side are also connected to the refrigerating chamber air duct tube 70 through a cooling fan 71 controlled by a solenoid valve. At the bottom of the condensate water outlet, a pipe is connected to the water inlet of the air conditioner cold air generator 76 at the top. 75 is connected; the air-conditioning cold wind generator 76 is a multi-pipe type for air-water exchange, with a fan 74 and an air-conditioning air supply pipe 73 on the side with solenoid valve control, and two pipes are set on the top of the air-water exchanger Mouth, one is from the bottom to the inlet 75 of the bottom of the gas-water exchanger, and one is the water outlet 77 connected to the water inlet 78 on the top of the water storage tank 80;
其中所述的储水罐 80是一个上设入水口 78, 侧设出水口 79的容器; 所述的低温制氮制热装置: 由三台涡流管式制冷机 87、 88、 89组成的涡流管
制冷机组、 由三台蒸汽发生器 90、 91、 92组成的蒸汽发生器组, 和一台蒸汽热水 储罐 115及管路组成; ■ The water storage tank 80 is a container with a water inlet 78 on the side and a water outlet 79 on the side; the low-temperature nitrogen heating device: a vortex composed of three vortex tube refrigerators 87, 88, and 89 Tube Refrigeration unit, a steam generator set consisting of three steam generators 90, 91, 92, and a steam hot water storage tank 115 and pipes; ■
其中所述的涡流管制冷机组是由三台涡流管式制冷机 87、 88、 89首尾串连相 接组成的, 第一台涡流管式制冷机 87的氮气入口 81与温差冷凝制水器的底部设 有两个的氮气出口 67、 69相并连,第一台涡流管式制冷机 87的氮气出口 82与第 二台涡流管式制冷机 88的氮气入口 83相连,第二台涡流管式制冷机 88的氮气出 口 84与第三台涡流管式制冷机 89的氮气入口 85相连, 第三台涡流管式制冷机 89的液氮出口 86与压力发生装置的等压位差注液器 1、 10顶部的液氮入口 3、 6 相并连; The vortex tube refrigerator unit is composed of three vortex tube refrigerators 87, 88, and 89 connected in series. The nitrogen inlet 81 of the first vortex tube refrigerator 87 and the temperature difference condensing water generator Two nitrogen outlets 67 and 69 are connected in parallel at the bottom. The nitrogen outlet 82 of the first vortex tube refrigerator 87 is connected to the nitrogen inlet 83 of the second vortex tube refrigerator 88, and the second vortex tube type The nitrogen outlet 84 of the refrigerator 88 is connected to the nitrogen inlet 85 of the third vortex tube refrigerator 89, and the liquid nitrogen outlet 86 of the third vortex tube refrigerator 89 is connected to the isobaric injector 1 of the pressure generating device 1 The liquid nitrogen inlets 3 and 6 at the top of 10 are connected in parallel;
其中所述带自动冷风排放阀 99、 108、 114的蒸汽发生器 90、 91、 92为套装 在三台涡流管式制冷机 87、 88、 89后面散热管 102、 110、 113上的中空式柱型 圆桶, 在圆桶上下球顶处各设一个通孔, 上通孔为蒸汽出口 93、 104、 112, 下通 孔为冷凝水入口 103、 111、 116; The steam generators 90, 91, and 92 with automatic cold air discharge valves 99, 108, and 114 are hollow columns that are mounted on the radiating tubes 102, 110, and 113 behind three vortex tube refrigerators 87, 88, and 89. Type barrels, one through hole is provided at the top and bottom of the barrel, the upper through holes are steam outlets 93, 104, 112, and the lower through holes are condensed water inlets 103, 111, 116;
其中所述蒸汽热水储罐 115为内设叁组螺旋换热盘管 105、 106、 107的中空 式上下球顶的柱型圆桶, 蒸汽热水储罐 115上球顶部设五个通孔, 其中三个通孔 为叁个螺旋换热盘管 105、 106、 107的蒸汽入口 94、 95、 97, 第四、 五通孔为由 电磁阀控制的蒸汽出口 96、 98; 在蒸汽热水储罐中上部设两个通孔, 其一为由电 脑控制的水位控制仪 100, 另一个为由电磁阀控制的开水出口 101;在蒸汽热水储 罐 115球顶侧中下方另设一个通孔为由电磁阀控制的热水出口 109, 蒸汽热水储 罐 115下球底部设四个通孔, 其中三个为冷凝水出口 117、 118、 119, 另一个通 孔为由电磁阀控制的自来水入口 120。 The steam hot water storage tank 115 is a hollow cylindrical barrel with three sets of spiral heat exchange coils 105, 106, and 107. The steam hot water storage tank 115 is provided with five through holes on the top of the ball. Among them, three through holes are steam inlets 94, 95, 97 of three spiral heat exchange coils 105, 106, 107, and the fourth and fifth through holes are steam outlets 96 and 98 controlled by solenoid valves; There are two through holes in the middle and upper part of the storage tank, one is a water level controller 100 controlled by a computer, and the other is a boiling water outlet 101 controlled by a solenoid valve. The hole is a hot water outlet 109 controlled by a solenoid valve. There are four through holes at the bottom of the lower part of the steam hot water storage tank 115, three of which are condensate water outlets 117, 118, and 119, and the other through hole is controlled by a solenoid valve. Tap water inlet 120.
其中三个蒸汽发生器 90、 91、 92上顶部蒸汽出口 93、 104、 112, 是通过管 路与蒸汽热水储罐 115内的叁组螺旋换热盘管 105、 106、 107上的蒸汽入口 94、 95、 97相连; 三个蒸汽发生器 90、 91、 92下部的冷凝水入口 103、 111、 116与 蒸汽热水储罐 115内的叁组螺旋换热盘管 105、 106、 107的冷凝水出口 117、 118、 119在底部相连后再与注水阀门 121、 122、 123相连。 The top steam outlets 93, 104, and 112 on the three steam generators 90, 91, and 92 are the steam inlets on the three sets of spiral heat exchange coils 105, 106, and 107 in the steam and hot water storage tank 115 The condensate inlets 103, 111, 116 of the lower part of the three steam generators 90, 91, 92 and the three sets of spiral heat exchange coils 105, 106, 107 in the steam hot water storage tank 115 are connected. Water outlets 117, 118, 119 are connected at the bottom and then connected to water injection valves 121, 122, 123.
所述低温压力发生装置中的气液交换器 16的氮气出口 13通过管路与温差冷 凝制水装置 B组温差冷凝制水器 53、 63的氮气入口 55、 61及等压位差注液器 1、 10的压力氮气入口 4、 8相连; The nitrogen outlet 13 of the gas-liquid exchanger 16 in the low-temperature pressure generating device passes through the pipeline and the temperature difference condensing water production device. The nitrogen inlets 55 and 61 of the temperature difference condensing water production device 53, 63 and the isobaric liquid injection device. 1, 10 pressure nitrogen inlets 4, 8 are connected;
所述压力发生装置的气液交换器 16液氮入口 18通过管路与等压位差注液器 Gas-liquid exchanger of the pressure generating device 16 Liquid nitrogen inlet 18 Through the pipeline and the isobaric liquid injector
1、 10底部由电磁阀控制的出液口 11、 12相连;
所述压力发生装置的气液交换器 16内螺旋换热盘管 15的上入口 14与所述气 轮机 28的氮气出口 27及与所述冷能发电装置的等压位差注液器 30、 29顶部的氮 气入口 20、 24相连; The outlets 11, 12 controlled by solenoid valves at the bottom of 1, 10 are connected; The upper inlet 14 of the spiral heat exchange coil 15 in the gas-liquid exchanger 16 of the pressure generating device, the nitrogen outlet 27 of the gas turbine 28, and the isobaric liquid injector 30 with the cold energy generating device, The nitrogen inlets 20 and 24 at the top of 29 are connected;
所述压力发生装置的气液交换器 16内螺旋换热盘管 15的下出口 17与所述冷 能发电装置的等压位差注液器 30、 29顶部氮入液口 19、 22相连; The lower outlet 17 of the spiral heat exchange coil 15 in the gas-liquid exchanger 16 of the pressure generating device is connected to the nitrogen inlets 19 and 22 at the top of the isobaric liquid injectors 30 and 29 of the cold energy generating device;
所述冷能发电装置的等压位差注液器 30、 29底部由电磁阀控制的出液口 31、 32并连后再与冷能发电装置的交叉组合的温差冷凝制水器 A组 52、 59底部由电 磁阀控制的两个液氮入口 66、 68相并连; The temperature difference condensing water generator A group 52 of the cold-energy power generation device isobaric liquid injectors 30, 29 at the bottom of which are controlled by solenoid valves, and then cross-combined with the cold-energy power generation device. The two liquid nitrogen inlets 66 and 68 controlled by solenoid valves at the bottom of 59 are connected in parallel;
所述冷能发电装置的气轮机 28的氮气入口 33与温差冷凝制水器 A组 52、 59 中的两个换热片式螺旋换热盘管 50、 58顶部的氮气出口 49、 57相并连; The nitrogen inlet 33 of the gas turbine 28 of the cold power generation device is parallel to the nitrogen outlets 49 and 57 at the top of the two heat exchange fin spiral heat exchange coils 50 and 58 in the group 52 and 59 of the temperature difference condensing water generator A. Even
所述温差冷凝制水装置温差冷凝制水器 B组 53、 63的散热片式换热排管 54、 62,下端由电磁阀控制的氮气出口 67、 69与所述低温制氮制热装置的第一台涡流 管式制冷机 87的氮气入口 81相并连; In the temperature difference condensing water production device, the fin-type heat exchange exhaust pipes 54, 62 in the temperature difference condensing water production device B group 53, 63, the nitrogen outlets 67, 69 at the lower end controlled by a solenoid valve, and the low temperature nitrogen heating heating device. The nitrogen inlets 81 of the first vortex tube refrigerator 87 are connected in parallel;
整个系统全部电磁阀和风机都由电脑系统 124自控进行交替开、 关, 其中低 温制氮制热装置的蒸汽热水储罐中的水位由蒸汽热水储罐侧上部的水位控制仪 100自控; 热风装置 35中的磁力换向装置 41中的电磁线圈的电磁磁场 44、 42由 电脑自控进行交替通、 断电源。 All solenoid valves and fans of the entire system are switched on and off automatically by the computer system 124. The water level in the steam hot water storage tank of the low-temperature nitrogen heating device is automatically controlled by the water level controller 100 on the side of the steam hot water storage tank. The electromagnetic fields 44 and 42 of the electromagnetic coil in the magnetic reversing device 41 in the hot air device 35 are controlled by a computer to alternately turn on and off the power.
所述系统内的低温压力发生装置的气液交换器 16、 等压位差注液器 1、 10; 冷能发电装置的气轮机 28、等压位差注液器 30、 29, 热风装置 35的壳体 40和温 差冷凝制水装置的连通风管 72、空调冷风发生器 76; 低温制氮制热装置的三个蒸 汽发生器 90、 91、 92、蒸汽热水储罐 115; 还包括所有输气管、输液管和风机 71、 74及风管 70、 73的所有外壳都必须由隔热材料隔热处理。 The gas-liquid exchanger 16, low-pressure injectors 1, 10 of the low-temperature pressure generating device in the system; the gas turbine 28, the constant-pressure injectors 30, 29, and the hot-air device 35 of the cold power generator Housing 40 and the connecting air pipe 72 of the temperature difference condensing water making device, the air conditioning cold air generator 76; the three steam generators 90, 91, 92 of the low temperature nitrogen heating device, and the steam hot water storage tank 115; also including all All casings of the gas pipes, infusion pipes and fans 71, 74 and the air pipes 70, 73 must be insulated with heat-insulating materials.
本发明的温差冷凝制水、 供热、 空调、 发电系统, 是这样工作的: 首先将等 压位差注液器 1、 30、 上部的注液阀门 2、 23、 用手开启并注满液氮再关上, 同时 将蒸汽热水储罐 115底部的冷凝水出口 117、 118、 119上的注水阀门 121、 122、 123、 再用手开启, 设在蒸汽发生器 90、 91、 92 中部的排气阀门 99、 108、 114 向蒸汽发生器 90、 91、 92内注一定量的水, 至从排气阀门 99、 108、 114流出水, 再用手关闭蒸汽热水储罐 115底部的冷凝水出口 117、118、119上的注水阀门 121、 122、 123和蒸汽发生器 90、 91、 92中部的排气阀门 99、 108、 114,至此开机前 准备工作完毕。 The temperature difference condensing water-making, heating, air-conditioning and power generation system of the present invention works as follows: Firstly, the isostatic pressure difference injector 1, 30, the upper injection valve 2, 23, are opened by hand and filled with liquid. The nitrogen is closed again, and at the same time, the water injection valves 121, 122, 123 on the condensate water outlets 117, 118, and 119 at the bottom of the steam hot water storage tank 115 are opened by hand, and the drains provided in the middle of the steam generators 90, 91, 92 Air valves 99, 108, 114 Fill a certain amount of water into the steam generators 90, 91, 92 until the water flows out from the exhaust valves 99, 108, 114, and then close the condensate at the bottom of the steam hot water storage tank 115 by hand The water injection valves 121, 122, and 123 on the outlets 117, 118, and 119 and the exhaust valves 99, 108, and 114 in the middle of the steam generators 90, 91, and 92 have been prepared before starting.
启动电脑控制系统,使等压位差注液器 1、 30底部由电磁阀控制的出液口 11、
31及顶部由电磁阀控制的氮气入口 4、 20和等压位差注液器 10、 29顶部的由电 磁阀控制的排气阀 9、 25及等压位差注液器 10、 29顶部的由电磁阀控制的液氮入 口 6、 22, 热风装置中的磁力换向装置和风机、 电加热器、 和连通管一端的风机 及空调冷风发生器的风机自控开启蒸汽热水储罐 115上侧面由水位控制仪 100自 控的蒸汽热水储罐 115顶部由电磁阀控制的蒸汽出口 96的阀门和底部的由电磁阀 控制的自来水入口 120 阀门, 同时开启, 使液氮经管路同时进入气液交换器 16 和温差冷凝制水装置的 A组温差冷凝制水器的下方的液氮入口内, 热风装置中的 磁力换向装置也同时每次间隙 10秒转换风机的热风方向,从而保证了系统正常进 行温差交换。 Start the computer control system, and make the outlets at the bottom of the isobaric liquid injectors 1, 30 controlled by a solenoid valve 11, 31 and nitrogen inlets 4, 20 controlled by solenoid valves and isobaric injectors 10, 29 At the top of solenoid valve controlled exhaust valves 9, 25 and isobaric injectors 10, 29 Liquid nitrogen inlets 6, 22 controlled by solenoid valves, magnetic reversing devices in hot air installations, fans, electric heaters, fans at one end of the connecting pipe, and fans of air-conditioning cold air generators. Automatically open the upper side of the steam hot water storage tank 115 The steam hot water storage tank 115 controlled by the water level controller 100 is controlled by a solenoid valve controlled by a solenoid valve at the top and a tap water inlet valve controlled by a solenoid valve at the bottom. The valve is opened at the same time, so that liquid nitrogen enters the gas-liquid exchange through the pipeline at the same time. In the liquid nitrogen inlet below the Group A temperature difference condensate water generator of the temperature difference 16 and temperature difference condensate water production device, the magnetic commutation device in the hot air device also changes the direction of the hot air of the fan at a gap of 10 seconds at the same time, thereby ensuring the normal system. Exchange temperature differences.
当全系统工作初始, 液氮从等压位差注液器 1底部由电磁阀控制的出液口 11 因降差进入温差冷凝制水装置的 A组温差冷凝制水器的换热片式螺旋换热盘管下 端的由电磁阀控制的氮气入口内, 并在换热片式螺旋换热盘管舜间吸热气化成常 温高压氮气, 经换热片式螺旋换热盘管的上端的由电磁阀控制的氮气出口及管路 经过气轮机带动发电机做功,同时进入等压位差注液器 30由电磁阀控制的氮气入 口对该等压位差注液器送压后,进入低温压力发生器 16内设的螺旋换热盘管内与 低温压力发生器内的液氮由上至下进行温差交换, 舜间失热降温冷凝成液氮, 被 压力所推经管路进入等压位差注液器 29顶部幵启由电磁阀控制的氮气入口注入 等压位差注液器 29内从而完成半程循环; When the whole system works initially, liquid nitrogen flows from the outlet 11 controlled by the solenoid valve at the bottom of the isobaric liquid injector 1 into the temperature difference condensing water generating unit of the temperature difference condensing water generating device. The nitrogen inlet at the lower end of the heat exchange coil is controlled by a solenoid valve, and heat is absorbed and vaporized in the heat exchange fin spiral heat exchange coil Shun to be normal temperature and high pressure nitrogen. The nitrogen gas outlet and pipeline controlled by the solenoid valve pass the gas turbine to drive the generator to perform work, and enter the equal pressure differential injector 30. The nitrogen inlet controlled by the solenoid valve sends pressure to the equal pressure differential injector and enters low temperature pressure. The temperature difference between the liquid nitrogen in the spiral heat exchanger coil inside the generator 16 and the low-temperature pressure generator is exchanged from top to bottom. The top of the liquid tank 29 is opened by a nitrogen valve controlled by a solenoid valve and injected into the liquid tank 29 of equal pressure difference to complete a half cycle;
于此同时低温压力发生器 16内的液氮舜间吸热气化, 温度控制在负 60°C的 高压氮气经顶部的出口首先进入等压位差注液器 1顶部的氮气入口, 向等压位差 注液器 1送压, 再经管路进入温差冷凝制水装置的 B组温差冷凝制水器的换热片 式螺旋换热盘管上端的由电磁阀控制的氮气入口内, 并在换热片式螺旋换热盘管 舜间吸热气化温度控制在负 20°C高压氮气, 最近经第三台涡流管式制冷机(每经 过一台降温 60°C ) 的三次降温降压后又成为液氮, 被压力所动回流等压位差注液 器 10顶部的液氮入口, 进入等压位差注液器 10, 也从而完成半程循环; At the same time, the liquid nitrogen in the low-temperature pressure generator 16 absorbs heat and gasifies, and the high-pressure nitrogen whose temperature is controlled at minus 60 ° C first enters the nitrogen inlet at the top of the isobaric liquid injector 1 through the outlet at the top. The pressure difference liquid injector 1 sends the pressure, and then enters the nitrogen inlet controlled by the solenoid valve at the upper end of the heat exchange fin spiral heat exchange coil of the group B temperature difference condensing water generator of the temperature difference condensing water device through the pipeline. The heat exchange fin spiral heat exchange coil Shunjian endothermic gasification temperature is controlled at minus 20 ° C high pressure nitrogen, and it has recently passed the third vortex tube refrigerator (each time 60 ° C) for three times of temperature reduction and pressure reduction. Then it becomes liquid nitrogen, and the liquid nitrogen inlet at the top of the isobaric liquid injector 10 is moved back by the pressure and enters the isobaric liquid injector 10, thereby completing the half cycle;
在液氮和低温氮气在温差冷凝制水装置的 A、 B组温差冷凝制水器内经过时, 产生的低温使装置周围空气舜间被吸附到换热片式螺旋换热盘管上结成冰霜, 在 定时换向装置的按时导入的由风机将电加热器产生的热流吹至换热片式螺旋换热 盘管上,使螺旋换热盘管上结成的冰霜舜间溶化成低温水, 流入连通风管内,一部 分低温被压力和吸引力经连通风管侧面的风机经管路送入冷冻库, 而低温水经底 部流入空调冷气发生器内, 在空调冷气发生器内的多管式气水交换器中再次强制
换热后, 升温成常温水, 在空调冷气发生器内水满溢出流入储水罐; When the liquid nitrogen and low-temperature nitrogen pass through the temperature difference condensing water generators of the group A and B of the temperature difference condensing water device, the resulting low temperature causes the air around the device to be adsorbed on the heat exchange sheet spiral heat exchange coils to form Frost, the heat flow generated by the electric heater is blown to the heat-exchanger fin spiral heat exchange coil by the fan which is introduced on time in the timing reversing device, so that the frost formed on the spiral heat exchange coil melts into low-temperature water. When it flows into the connecting duct, a part of the low temperature is pressured and attracted by the fan on the side of the connecting duct to the freezer through the pipeline, and the low-temperature water flows into the air-conditioning cold air generator through the bottom, and the multi-pipe air in the air-conditioning cold air generator Forced again in the water exchanger After the heat exchange, the temperature rises to normal temperature water, and the water in the air-conditioning cold air generator overflows and flows into the water storage tank;
在负 60Ό的高压氮气温差冷凝制水装置的 B组温差冷凝制水器经过后, 吸热 气温度控制在负 20°C高压氮气, 最近经第三台涡流管式制冷机(每经过一台降温 60°C ) 的三次降温降压后又成为液氮的同时, 三台涡流管式制冷机后部套装的带 自动冷风排放阀的三台蒸汽发生器内的三个散热管同时吸热产生蒸汽, 经管路进 入蒸汽热水罐顶部再进入到蒸汽热水罐内叁组螺旋换热盘管, 在蒸汽热水罐内由 上至下进行热交换, 放热又冷凝成水被再次因水位差压入三台蒸汽发生器内的三 个散热管再次循环蒸发换热, 而此时蒸汽热水罐内的低温水因吸热而升温汽化产 生 13CTC的高温, 此时蒸汽热水罐顶部的与热风装置内的蒸汽加热器的蒸汽入口 相连的由电磁阀控制的出口自动开启, 向蒸汽加热器供热, 同时热风装置内的电 加热器自动关闭, 此时蒸汽热水罐将自动向外供蒸汽或开水热水; After the Group B temperature difference condensing water generator of the high-pressure nitrogen temperature difference condensing water generating device of minus 60Ό passed, the endothermic gas temperature was controlled at a high pressure nitrogen of minus 20 ° C. Recently, the third vortex tube refrigerator (each passing one After cooling down to 60 ° C for three times, the temperature and pressure became liquid nitrogen. At the same time, three vortex tubes in the rear of three vortex tube refrigerators with automatic cold air discharge valves and three heat generators in the three steam generators absorb heat simultaneously. The steam enters the top of the steam hot water tank through the pipeline and then enters the three sets of spiral heat exchange coils in the steam hot water tank. Heat is exchanged from top to bottom in the steam hot water tank, and the heat is condensed into water, which is again caused by the water level. The three heat-radiating pipes in the three steam generators are cyclically evaporated and exchanged again. At this time, the low-temperature water in the steam hot water tank is heated and vaporized due to heat absorption, resulting in a high temperature of 13CTC. The outlet connected to the steam inlet of the steam heater in the hot air device is automatically opened to supply heat to the steam heater. At the same time, the electric heater in the hot air device is automatically turned off. At this time, the steam hot water tank Automatic water or steam for hot water out;
待等压位差注液器 1、 30内的液氮流尽, 电脑将自控关闭等压位差注液器 1、 30底部由电磁阀控制的出液口 11、 31及顶部由电磁阀控制的氮气入口 4、 20和 等压位差注液器 10、 29顶部的由电磁阀控制的排气阀 9、 25及等压位差注液器 10、 29顶部的由电磁阀控制的液氮入口 6、 22, 并同时开启等压位差注液器 10、 29底部由电磁阀控制的出液口 12、 32及顶部由电磁阀控制的氮气入口 8、 24和 等压位差注液器 1、 30顶部的由电磁阀控制的排气阀 5、 21及等压位差注液器 1、 30顶部的由电磁阀控制的液氮入口 3、 19, 等压位差注液器 1、 30顶部的由电磁 阀控制的排气阀 5、 21使氮气与液氮进行无能耗自控循环做功。 After the liquid nitrogen in the isobaric injectors 1 and 30 runs out, the computer will automatically close the isobaric injectors 1, 30 at the bottom, which are controlled by solenoid valves. Nitrogen inlets 4, 20 and constant pressure differential injectors 10, 29 top of solenoid valve controlled by solenoid valve 9, 25 and constant pressure differential injectors 10, 29 top of liquid nitrogen controlled by solenoid valve Inlet 6, 22, and open the constant pressure differential injectors 10, 29 at the same time. Outlet ports 12, 32 controlled by solenoid valves at the bottom and nitrogen inlets 8, 24 and equal pressure differential injectors controlled by solenoid valves at the top. 1. The exhaust valve 5, 21 at the top of the solenoid valve controlled by the solenoid valve 5, 21 and the isobaric injector 1, the liquid nitrogen inlet 3, 19 at the top by the solenoid valve controlled by the solenoid valve, 1. The exhaust valves 5 and 21 controlled by solenoid valves at the top of 30 enable nitrogen and liquid nitrogen to perform self-controlling cycles without energy consumption.
本发明的工作原理如下: 本发明是利用 "热很难向下传导的现象" 以环境温 度为 "高温热源"人为的制造一个 "低温热源"液氮, 利用氮气与液氮之间的温 差, 按照 "闭路循环"方法, 进行无能耗自控循环做功。 The working principle of the present invention is as follows: The present invention artificially manufactures a "low-temperature heat source" liquid nitrogen using "the phenomenon that heat is difficult to conduct downwardly" with an ambient temperature of "high-temperature heat source", and uses the temperature difference between nitrogen and liquid nitrogen. In accordance with the "closed loop" method, a non-energy-consumption self-controlled cycle is performed to perform work.
工业应用性 Industrial applicability
本发明提供的温差冷凝制水、 供热、 空调、 发电系统, 是利用 "闭路循环" 理论设计的, 运行时无能耗, 只须一次性启动冷能, 利用空气中的自然热源, 即 可在冷凝空气制水的同时提供热风、 冷风、 蒸汽和电力, 使沙漠和高原等干旱缺 水或冷、 热无常或缺少电力的地区, 得到干净廉价的冷、 热水和冷、 热风及充足 的电力。 本发明具有广阔的工业应用前景。
The temperature difference condensation water production, heating, air conditioning, and power generation systems provided by the present invention are designed using the "closed circuit" theory, and there is no energy consumption during operation. Only cold energy needs to be started at one time, and natural heat sources in the air can be used. Condensing air to produce water while providing hot air, cold wind, steam and electricity, so that dry and lack of water or cold, hot or lack of electricity in deserts and plateaus, get clean and cheap cold, hot water and cold, hot air and sufficient power . The invention has broad industrial application prospects.