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    • 3. 发明专利
    • Brine desalting device
    • 葡萄酒脱盐装置
    • JPS5763189A
    • 1982-04-16
    • JP13801880
    • 1980-10-01
    • Mitsubishi Electric Corp
    • KUSAKAWA HIDEAKIKAI JIYUNJIROU
    • C02F1/04B01D3/00
    • Y02A20/128
    • PURPOSE: To improve the utilization efficiency of energy required for desalting by isolating a condensing section and an evaporating section by isolating a condensing section and an evaporating section by means of partition walls, and transferring heat from the condensing section to the evaporating section via the partition walls.
      CONSTITUTION: In an evaporating section 1, brine contacts the carrier gas ascending from below, and steam and thermal energy are carried by this carrier gas. Further, the brine falls downward while wetting a partition wall 4 and heat exchanging fans 41, and is discarded from a discharge pipe 9. The carrier gas absorbing the thermal energy is fed via a circulation pipe 11 to a condensing section 2 by a blower 10. While it is descending in the section 2, it condenses steam and releases heat. In the section 2, the heat released in acordance with the condensation of the steam is recovered by the partition wall 4, 5, and the fins 41, 51, and is converted to sensible heat or the latent heat of evaporation in a water temp. elevating section 3 and the section 1.
      COPYRIGHT: (C)1982,JPO&Japio
    • 目的:通过隔离冷凝段和蒸发段,通过隔离隔离冷凝段和蒸发段来提高脱盐所需能量的利用效率,并通过隔板将热量从冷凝段传递到蒸发段 墙壁 构成:在蒸发段1中,盐水接触从下方升起的载气,蒸汽和热能由载气承载。 此外,盐水向下倾斜,同时润湿分隔壁4和热交换风扇41,并从排放管9中丢弃。吸收热能的载气通过循环管道11通过鼓风机10供给到冷凝段2 虽然在第2部分下降,它会冷凝蒸汽并释放热量。 在第2部分中,依靠蒸汽冷凝释放的热量被分隔壁4,5和散热片41,41回收,并在水温中转化为显热或蒸发潜热。 升降部分3和部分1。
    • 4. 发明专利
    • Heat accumulator
    • 热量累加器
    • JPS5726390A
    • 1982-02-12
    • JP10094280
    • 1980-07-22
    • Mitsubishi Electric Corp
    • KIMURA HIROSHIKAI JIYUNJIROU
    • F28F23/02F28D17/00F28D20/00
    • Y02E60/142
    • PURPOSE: To enable the improvement of a radiation rate of an air conditioner utilizing a fusion latent heat, by method wherein traps are attached at the inside of a heat accumulating vessel, and this prevents falling of crystal particles of a heat accumulating material.
      CONSTITUTION: Circular projecting edges 2, acting as a trap, are attached at equal intervals at the inside of a cylindrical vessel. This causes adhering of crystal particles, dropping from above to the edges 2 at a curing time. As a result, the crystal particles in the vessel 1 increases, and a radiation speed accelerates. At a fusion time as well, crysral reaction products in a fusion heat accumulating material are easy to settle down to the edges 2, and nuclear products are apt to reduce at a curing time. This enables the acceleration of a curing rate, the improvement of uniformalization of a heat accumulating component, and the improvement of a heat cycle stability.
      COPYRIGHT: (C)1982,JPO&Japio
    • 目的:为了提高利用熔融潜热的空调机的放射率,通过在蓄热容器的内部附着有捕集器的方法,能够防止蓄热材料的结晶粒子的落下。 构成:作为捕集器的圆形突出边缘2以相等的间隔连接在圆柱形容器的内部。 这导致结晶颗粒的粘附,在固化时从上方落到边缘2。 结果,容器1中的晶体颗粒增加,辐射速度加快。 在融合时间,熔融聚集材料中的冷冻反应产物易于沉降到边缘2,核产品在固化时易于降低。 由此,能够加速固化速度,提高蓄热部件的均匀化,提高热循环的稳定性。
    • 10. 发明专利
    • BRINE DESALINATING DEVICE HAVING HEAT RECOVERING FUNCTION
    • JPS57162689A
    • 1982-10-06
    • JP4912781
    • 1981-03-30
    • MITSUBISHI ELECTRIC CORP
    • KUSAKAWA HIDEAKIKAI JIYUNJIROUMATSUOKA HIROMASA
    • C02F1/04F28F3/00
    • PURPOSE:To increase efficiency of utilization of energy required for desalination of brine by moving latent heat liberated in a condensation section to a brine heating section and an evaporation section through a partition plate and moving carrying gas from the evaporation section to the condensation section. CONSTITUTION:Raw brine is supplied to a brine heating section 3 through an inlet port 11 of the device. The brine is heated by heat of condensation of steam etc. in the condensation section 4 transmitted through a conductive partition plate 2 while going upward in the heating section 3 and flows out from a discharge port 9. This brine is passed through a solar heat collector or a suitable waste heat boiler to make its temperature below 100 deg.C at atmospheric pressure and spurted from a hot brine shower 10. On the other hand, carrying gas is sent in from a blowing port 14 to evaporate water in the hot brine. Meanwhile, latent heat etc. are supplied from the condensation section 4 to the evaporation section 5 through the partition plate 2. Pure water and carrying gas are taken out from an outlet port 12 of the condensation section 4. Waste brine is taken out from an outlet port of the evaporation section 5.