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    • 93. 发明专利
    • Extractive separation apparatus
    • 提取分离装置
    • JPS61129003A
    • 1986-06-17
    • JP24957484
    • 1984-11-28
    • Hitachi Ltd
    • SUGAI HIROSHIYOSHIDA MASAHIROTAKAKUSAKI TSUNEHIKOSATO JOSHIROTAKAHASHI SANKICHIMATSUZAKI HARUMI
    • A23L27/10B01D11/02C10G1/04C10G21/00C11B9/00C11B9/02C12N9/00
    • PURPOSE: To extract and separate an objective substance with high efficiency, by enabling the change-over of extraction tanks and continuously extracting a substance to be extracted while independently controlling the pressures and temps. in the extraction tanks and a separation tank.
      CONSTITUTION: After an objective substance was introduced into an extraction tank 27A, the fluid of a fluid source 1 is allowed to gradually fill the whole of the system through pipings 2, 3, 6, 14. Next, a liquefier 53 is operated to liquefy the fluid. Subsequently, the substance to be extracted, which was extracted in the extraction tank 27A, is mixed with an super-critical fluid to be sent to a separation tank 34 where the fluid is separated from the extracted substance to be sent to a gassification tank 48. The fluid issued from the gassification tank 48 is passed through the liquefier 53 to be perfectly liquefied and sent to a recirculation pump 10 to be recycled and utilized. Further, the extraction time of the objective substance in the extraction tank or the extraction amount of the objective substance in the separation tank is set as a change- over condition and the change-over of extraction tanks 27A, 27B is performed by a change-over control mechanism consisting of automatic valves 19A, 19B, 28A, 28B.
      COPYRIGHT: (C)1986,JPO&Japio
    • 目的:高效率提取和分离目标物质,可独立控制压力和温度,能够切换提取罐,连续萃取提取物质。 在提取罐和分离罐中。 构成:将目标物质引入提取槽27A后,允许流体源1的流体通过管道2,3,6,14逐渐填充整个系统。接下来,液化器53被操作以液化 流体。 随后,将在提取槽27A中提取的待提取物质与超临界流体混合,送至分离槽34,在该分离槽34中,将被萃取的物质与流出的物质分离,送至气化槽48 来自放气罐48的液体通过液化器53被完全液化并送到再循环泵10中以便再循环使用。 此外,将提取罐中的目标物质的萃取时间或分离罐中的目标物质的提取量设定为转换条件,并且提取罐27A,27B的转换通过改变条件进行, 控制机构由自动阀19A,19B,28A,28B组成。
    • 94. 发明专利
    • Crude oil storage apparatus
    • 原油储存装置
    • JPS6119689A
    • 1986-01-28
    • JP14111484
    • 1984-07-06
    • Hitachi Ltd
    • TAKAKUSAKI TSUNEHIKOSATOU JIYOUSHIROUYOSHIDA MASAHIROTAKAHASHI SANKICHIMATSUZAKI HARUMIMUTSUKUSHI TOSHIKI
    • C10G31/08B65D90/00
    • PURPOSE: To prevent sludge in a tank from settling and being accumulated, by controlling the temp. of charge water charged at the bottom of a crude oil storage tank and the concn. of salts.
      CONSTITUTION: Crude oil 6 from a tanker is introduced through a pipe 9 and an inner pipe 17 into a crude oil storage tank 2 in which charge water 7 is charged. The temp. of the charge water 7 in the tank 2 is detected by a water temperature detector 15, a heater 15 is operated and controlled through a temperature controlling device 14 on the basis of the detected values to thereby keep the temp. of the charge water at a temp. higher than the m.p. (40W70°C) of waxes in the crude oil 6, whereby the waxes are dissolved and diluted with water and salt water droplets and fine inorg. matters are precipitated. The charge water 7 is fed through a circulating pump 11 and an oil/water separator 12 to a desalting device 13 where the charge water 7 is desalted to such an extent that electrical conductivity is reduced to 500μΩ/cm or below. The desalted water is then recycled to the tank 2.
      COPYRIGHT: (C)1986,JPO&Japio
    • 目的:通过控制温度,防止油箱内的污泥沉降和积聚。 装在原油储罐底部的充水水 的盐。 构成:来自油罐车的原油6通过管道9和内管道17引入原油储存罐2,原油储存罐2中装入加料水7。 温度 通过水温检测器15检测罐2内的装料水7,通过温度控制装置14根据检测值对加热器15进行操作和控制,从而保持温度。 的充电水在一个温度。 高于m.p. (40-70℃)的蜡,由此蜡溶解并用水和盐水滴稀释并精细化。 事情沉淀。 加料水7通过循环泵11和油/水分离器12输送到脱盐装置13,在该脱盐装置13中,加料水7脱盐至使导电率降至500muOMEGA / cm以下的程度。 然后将脱盐水再循环到罐2中。
    • 95. 发明专利
    • EXTRACTING SEPARATION DEVICE
    • JPS60187303A
    • 1985-09-24
    • JP4334684
    • 1984-03-07
    • HITACHI LTD
    • TAKAKUSAKI TSUNEHIKOSATOU JIYOUSHIROUYOSHIDA MASAHIROTAKAHASHI SANKICHIMATSUZAKI HARUMI
    • B01D11/02B01D11/04
    • PURPOSE:To enable control of pressure and temp. of an extraction tank and a separation tank independently and highly accurately by providing a temp. controlling mechanism and a pressure controlling mechanism respectively to the extraction tank and the separation tank. CONSTITUTION:An object material to be extracted and separated is charged to an extraction tank 28 and the fluid in a fluid source 21 is filled in the whole part of the system, and the extraction tank 28 is brought to a supercritical condition. The pressure is controlled by a pressure controlling valve 25, and the temp. is controlled to the coincide with a target temp. of a temp. indicator TR1 by circulating the fluid in the extraction tank using a combination of a heat exchanger 26 and a pump 27; thus, the pressure and the temp, are controlled independently to each other. The fluid mixture consisting of the extracted material and the fluid under the supercritical condition is sent to a separation tank 29, where the pressure is reduced to near a target pressure of the separation tank 29 by a reducing valve 50; the pressure is further controlled by a fine pressure controlling mechanism comprising a hydraulic survo motor 30, accumulator 36, etc. The temp. is further controlled so as to coincide with a target temp. of a temp. indicator TR2 by circulating the fluid mixture in the separation tank using a combination of a heat exchanger 31 and a pump 32.