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    • 3. 发明申请
    • GAS CONDENSER
    • 气体冷凝器
    • WO02008659A1
    • 2002-01-31
    • PCT/NO2001/000316
    • 2001-07-23
    • B01D5/00F17C13/00F25J1/00
    • F17C13/00B01D5/0021B01D5/0027F17C2265/032Y10S165/162
    • Gas condenser (2) arranged to condense gas/vapour (4) evaporating from a volatile liquid (6) being stored, for example, in a storage tank. The gas/vapour (4) is conducted into a gas chamber (16) provided with openings, possibly also nozzles (76), the gas chamber (16) being placed in a surrounding housing (36). Thereafter, the gas/vapour (4) is sucked into at least one venturi section (62, 64), wherein the liquid (6), for example, is flowing with a static underpressure relative to the inflowing gas/vapour (4). Via at least one expansion section (88, 90), a mixture (92) of gas/vapour (bubbles) (4) and liquid (6) flows onward to a condensing chamber (98), through which the static pressure of the liquid (6) increases and the gas/vapour (4) is condensed, after which the mixture (92) is conducted back to, for example, the storage tank. By means of one or several adjusting devices arranged to the gas condenser (2), the shape of the slot volume of the venturi section(s) (62, 64), possibly also the slot volume of expansion section(s) (80, 90), and thus the course of pressure through it/them, may be optimally adjusted/changed/adapted to the current operating condition and the current gas condensing need.
    • 用于冷凝从例如储存在储罐中的挥发性液体(6)蒸发的气体/蒸气(4)的气体冷凝器(2)。 气体/蒸气(4)被传导到设置有开口的气室(16)中,可能还有喷嘴(76),气室(16)被放置在周围的壳体(36)中。 此后,气体/蒸汽(4)被吸入至少一个文丘里管部分(62,64),其中液体(6)例如相对于流入的气体/蒸气(4)以静态负压流动。 通过至少一个膨胀部分(88,90),气体/蒸汽(气泡)(4)和液体(6)的混合物(92)向前流向冷凝室(98),液体的静压 (6)增加并且气/蒸气(4)被冷凝,之后混合物(92)被传导回到例如储罐。 通过布置到气体冷凝器(2)的一个或几个调节装置,文丘里管部分(62,64)的狭槽容积的形状,也可能是膨胀部分(80)的狭槽体积, 90),因此通过它们的压力的过程可以被最佳地调整/改变/适应于当前操作条件和当前的气体冷凝需求。
    • 4. 发明申请
    • HEAT EXCHANGER
    • 热交换器
    • WO1989008813A1
    • 1989-09-21
    • PCT/DK1989000024
    • 1989-02-09
    • F.L. SMIDTH & CO. A/SANDREASEN, Ole
    • F.L. SMIDTH & CO. A/S
    • F28C03/12
    • C04B7/432B04C3/00B04C5/00B04C5/081B04C5/103B04C5/12F23K1/04F27B15/003Y10S165/162
    • A heat exchanger in the form of a vessel for heat exchange of a pulverulent solid material and a gas, e.g. for preheating raw materials prior to a burning process by use of the hot exit gases fed to the vessel consists of a hollow cylindrical central part (1) with a tangential gas inlet (3), a conical base (2) with a material outlet (5), and a downwardly orientated gas outlet (4), a concave upper part (7, 7') facing the central part and with at least one material inlet (8); the downwardly orientated gas outlet (4) is mounted initially axially as a central pipe inside the vessel and is provided with a skirt (6); the height of the upper part, the distance of the material inlet from the vertical axis of the heat exchanger and the inclination of the inlet to the horizontal plane, the height of the central pipe gas inlet (4) above the lower end level of the central part (1) of the vessel and the inclination of the skirt (6) are all dimensioned so as to provide optimum conditions, partly for heat exchange in radial countercurrent between material and gas, partly for separation of material from gas inside the vessel due to the downwardly orientated axial and tangential gas velocities.
    • 用于热交换粉状固体材料和气体的容器形式的热交换器,例如, 用于通过使用供给到容器的热出口气体在燃烧过程之前预热原料由具有切向气体入口(3)的中空圆柱形中心部分(1),具有材料出口的锥形基座(2) 5)和向下定向的气体出口(4),面向中心部分的凹上部(7,7')和至少一个材料入口(8); 向下定向的气体出口(4)首先作为中心管轴向安装在容器内部并且设置有裙部(6); 上部的高度,材料入口与热交换器的垂直轴线的距离以及入口到水平面的倾斜度,中心管道气体入口(4)的高度在下端的高度 容器的中心部分(1)和裙部(6)的倾斜度都被设计为提供最佳条件,部分用于在材料和气体之间的径向逆流中的热交换,部分地用于将材料与容器内的气体分离, 到向下定向的轴向和切向气体速度。