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    • 83. 发明专利
    • MOLDING AND CARRYING-OUT EQUIPMENT FOR DRY ICE
    • JPH05116927A
    • 1993-05-14
    • JP28478691
    • 1991-10-30
    • MITSUBISHI HEAVY IND LTD
    • TAKEUCHI YOSHIYUKIKOBAYASHI KAZUTO
    • B01D53/62C01B31/36C01B32/55
    • PURPOSE:To enhance treatment efficiency by directly mixing gaseous carbon dioxide contained in a combustion exhaust gas with low-temperature gas, and compressing, molding and carrying the produced dry ice with a screw feeder. CONSTITUTION:The concentration of gaseous carbon dioxide contained in combustion exhaust gas is very low, about 5-10mol%. This is directly brought into contact with low-temperature cooling gas which has been heat-exchanged with a cryogenic source such as an LNG cryogen. However, produced dry ice is fine particles of about 1-300mum. Such a state is formed that these fine particles are floated in a large amount of exhaust gas. The fine particles are supplied to a screwfeeder 12 from a hopper 11. The screw of this feeder 12 is tilted and made gradually smaller. The fine particles of dry ice supplied into a groove are gradually compressed and molded into large particle diameter. The molded dry ice is passed through a hopper 13 and regulated to uniform flow rate by a second screw feeder 14. Then this is regulated to one block quantity of dry ice by a rotary valve 15 and thereafter led to a storage tank.
    • 84. 发明专利
    • MEMBRANE SEPARATION EQUIPMENT FOR AQUEOUS SOLUTION
    • JPH04354520A
    • 1992-12-08
    • JP12965391
    • 1991-05-31
    • MITSUBISHI HEAVY IND LTD
    • TAKEUCHI YOSHIYUKI
    • B01D61/36B01D65/00C02F1/48C02F9/00
    • PURPOSE:To increase permeation velocity without much changing the form of equipment and without causing much change in properties of the raw mate rial, such as heat and pressure by arranging equipment having the magnetization function in an aqueous solution feed supplying line to membrane separation equipment. CONSTITUTION:An aqueous solution feed in a raw material tank 1 is supplied to a magnetization equipment 4 through a line 2 by a feed supplying pump 3. Part of magnetized feed is returned to the raw material tank 1 through a line 5 and the greater part of it is supplied to a membrane equipment 7 through a line 6. A valve 8 and a valve 9 are installed in the line 5 and in the line 6 respectively to control the flow rate. In the membrane separation equipment 7, components permeating the membrane is introduced into a cold trap 11 through a line 10 where low boiling condensing components are condensed or solidified to separate them from noncondensable components and recovered. The noncondesable components are sucked from a line 12 by a vacuum pump 13, discharging from a line 14. Components not permeating the separation membrane are returned to the raw material tank 1 through a line 15.
    • 89. 发明专利
    • Multi-stage flash desalinator
    • 多级闪光脱盐机
    • JPS59169591A
    • 1984-09-25
    • JP4508683
    • 1983-03-17
    • Mitsubishi Heavy Ind Ltd
    • TAKEUCHI YOSHIYUKIKOKUBO RIYOUICHIIWAHASHI HIDEO
    • B01D3/06C02F1/06
    • B01D3/065Y02A20/128
    • PURPOSE:To enable to hold and adjust interstage pressure difference over a wide range, by making the height of a weir vertically provided on the bottom plate of an evaporation chamber at each stage lower by stages toward a low-temp. stage. CONSTITUTION:A round orifice 31, for instance, is adopted, and the height of a weir 24 vertically provided on the bottom plate 26 of an evaporation chamber 21a, 21b at each stage is made lower as l2>l3 by stages toward a low-temp. stage. Hereon, interstage pressure difference P1-P2 rises with the increase of the height l2 of the weir 24. Consequently, the desalinator can be made to cope with the interstage pressure difference over a wide range by changing the height l2, so that it becomes possible to deal with the large fluctuation in a load of evaporation.
    • 目的:通过使各级蒸发室底板上垂直设置的堰的高度逐级向低温,使得能够在较宽的范围内保持和调节级间压力差。 阶段。 构成:例如采用圆形孔31,并且在各级的蒸发室21a,21b的底板26上垂直设置的堰24的高度逐渐朝向低压侧逐渐降低, 温度。 阶段。 因此,级间压力差P1-P2随着堰24的高度l2的增加而上升。因此,通过改变高度l2,可以使脱水器能够在宽范围内处理级​​间压力差,使得可能 以处理蒸发量大的波动。