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    • 12. 发明专利
    • Installing method of turbine
    • 涡轮安装方法
    • JPS6114404A
    • 1986-01-22
    • JP13318384
    • 1984-06-29
    • Hitachi Ltd
    • MIZUNIWA SEIYOKOYAMA HIROSHI
    • F01D25/28
    • F01D25/28
    • PURPOSE:To raise a degree of accuracy in centering adjustment, by lowering the push-up force of a condenser supporting spring in time of turbine installation on a spring frame, and converting this force into an increment portion of water load on a condenser in time of operation, thereby performing a centering job. CONSTITUTION:A deck 6 is mounted on a pillar 7 via a spring 8, while turbines 1 and 2 and a generator 3 are installed on this deck. A condenser 4 is supported by a spring 9. These turbines are instaled in the following processes that first, frame pillars are set up, springs are set and locked, and concrete placing of the deck 6 takes place, then the turbine generator is installed there. Next, condenser water load equivalent to that in an operating load is imposed on each frame with the spring 9 adjusted, and afterward, the frame spring 8 is released and adjusted properly, thus coupling centering adjustment takes place.
    • 目的:通过降低涡轮机安装在弹簧架上的冷凝器支撑弹簧的上推力,提高中心调整精度,并将该力在时间上转换为冷凝器上的水负荷增量部分 的操作,从而执行定心作业。 构成:甲板6通过弹簧8安装在支柱7上,而涡轮机1和2以及发电机3安装在该甲板上。 冷凝器4由弹簧9支撑。这些涡轮机安装在以下过程中,首先框架柱被安装,弹簧被固定和锁定,并且进行甲板6的混凝土浇筑,然后将涡轮发电机安装在那里 。 接下来,调整与弹簧9相对应的运转负荷中的冷凝器水负荷,之后将框架弹簧8释放并适当调整,由此发生耦合对中调整。
    • 13. 发明专利
    • Modification of coal
    • 煤的修改
    • JPS5918796A
    • 1984-01-31
    • JP12581082
    • 1982-07-21
    • Hitachi Ltd
    • HISAIE TOSHIOYOKOYAMA HIROSHINOKITA SHIYUNSUKENAKAMURA YOUICHIMUROI KATSUMI
    • C10L9/02C10L9/00C10L9/08C10L9/10
    • C10L9/10C10L9/00
    • PURPOSE: To obtain a high colorific value coal with low water content even after transportation and/or storage, by distilling off tar from coal while dehydrating the coal, followed by coating the vapor of said tar on the surface of the coal.
      CONSTITUTION: Tar is distilled out of coal while carrying out a heat treatment for the coal, most preferably at 350W450°C. Said tar is evaporated into its vapor, which is then subjected to coating on the surface of the heat-treated coal under such a condition that the temperature difference between the vapor and the heat-treated coal may normally be 150W300°C, thus obtaining the objective modified coal. The amount of the tar distilled out of the coal is, in general, 4W 12wt% on the dry basis.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:即使在运输和/或储存后也能获得低含水量的高含量煤,通过在脱硫煤的同时蒸除煤中的焦油,然后在煤表面涂覆所述焦油的蒸气。 构成:对煤进行热处理,焦油从煤中蒸馏出来,最优选在350-450℃。 所述焦油蒸发成蒸气,然后在蒸气和热处理煤之间的温差通常为150-300℃的条件下,将其经受热处理煤表面的涂覆, 从而获得客观的改性煤。 从煤中蒸馏的焦油的量通常为干燥基础的4-12重量%。
    • 16. 发明专利
    • OXYGEN-CONCENTRATING METHOD
    • JPS57105220A
    • 1982-06-30
    • JP18204180
    • 1980-12-24
    • HITACHI LTD
    • YAHAGI TOSHIOTOMOMURA MASAOMIYOKOYAMA HIROSHIOOTANI KOUJINOKITA SHIYUNSUKE
    • B01D53/04B01D53/02C01B13/02
    • PURPOSE:To increase the concentration and the yield of O2 gas product by controlling the flow rate of air introduced into an adsorption tower, in a continuous oxygen- concentrating method wherein adsorption of N2 by introducing air into a plurality of adsorption towers, desorption of N2 by reducing a pressure, and equalization of pressure are sequentially repeated. CONSTITUTION:When conducting N2 adsorption and N2 desorption respectively in adsorption towers 1 and 2, solenoid valves 8, 10, 15 are opened and solenoid valves 9, 11, 16-18 are closed. In this condition, air is fed into a throttle plate 6 through a compressor 4 to adjust its flow rate, then it is fed into the tower 1, where N2 is adsorbed and O2 is fed into a pressure-equalizing tank 13. Thereafter, O2 is taken out through a pipe 14. On the other hand, N2 adsorbed in the tower 2 in a previous step is discharged through the solenoid valve 15 and a pipe 19 while returning the pressure of N2 to the atmospheric pressure. After the desorption of N2 in the tower 2 is completed, the valve 17 is opened and valves 9, 11, 15 are closed, then O2 in a compressed state in the tank 13 is introduced into the tower 2 and the pressure is equalized. Thereafter, adsorption and desorption of N2 are conducted respectively in the towers 2 and 1, in which case the throttle plate 6 prevents a large amount of air from flowing instantaneously into the adsorption tower at the time of adsorption, and the purposes can be attained.
    • 17. 发明专利
    • PRODUCTION OF POLYESTER
    • JPS56112926A
    • 1981-09-05
    • JP1595580
    • 1980-02-14
    • HITACHI LTD
    • YOKOYAMA HIROSHIHISAIE TOSHIONOKITA SHIYUNSUKESANO TSUYOSHI
    • C08G63/00C08G63/78
    • PURPOSE:To obtain a polyester economically, by a method wherein in carrying out a solid-phase polycondensation of a polyethylene terephthalate polymer, an inert gas to be passed through the polymn. mixt. is recycled for use, and at the same time the inert gas is used as a purge gas for desorption and regeneration in an adsorption tower. CONSTITUTION:A particulate polyethylene terephathalate polymer is continuously supplied from a hopper 2 to a solid-phase polycondensation reactor 1, and subjected to a solid-phase polycondensation reaction, and an inert gas is supplied to the lower part of the reactor 1 to remove impurities such as acetaldehyde. The inert gas is purified in an adsorption tower 7 for purification, and recycled for use. Just before the adsorbent of the adsorption tower 7 is saturated with impurities, gas flow is switched. A fresh inert gas is supplied through a conduit 11. The inert gas which bas passed through the reactor 1, is used as a purge gas for desorption and regeneration in the adsorption tower 7, whereby the amount of the inert gas to be used is reduced to the min. amount and the polyester can be obtd. economically.
    • 19. 发明专利
    • METHOD AND APPARATUS FOR CONCENTRATING OXYGEN FROM AIR
    • JPS5654208A
    • 1981-05-14
    • JP13000879
    • 1979-10-11
    • HITACHI LTD
    • YOKOYAMA HIROSHITOMOMURA MASAOMIYAHAGI TOSHIOOOTANI KOUJINOKITA SHIYUNSUKE
    • B01D53/04C01B13/02C01B21/02C01B21/04
    • PURPOSE:To enhance the O2 concn. and a yield ratio to a large extent by a method wherein, in concentrating O2 in air, the first adsorbing agent for adsorbing N2 and the second adsorbing agent for adsorbing O2 are packed in an adsorbing agent packing tower in a predetermined amount and the adsorbed O2 of the second adsorbing agent is utilized whtn the N2 adsorbing agent is regenerated under vacuum. CONSTITUTION:The second adsorbing agent 2 for selectively adsorbing O2 such as a synthetic zeolite 4A type is packed in a zone 2 within a pressure packing tower 1 and the first adsorbing agent for selectively adsorbing N2 such as a synthetic molybdenite is packed in a zone 3 and a check valve 5, a stock material air inlet pipe 4 having a solenoid valve 6, a concentrated O2 outlet pipe 7 having a sloenoid valve 9 and a timer 13 are arranged to constitute an apparatus as well as the amount of the second adsorbing agent is regulated so as to adsorb O2 smaller than the O2 amount after the air is passed through the first adsorbing agent. When the first adsorbing agent is subjected to the vacuum regeneration, the valve is switched by the timer 13 to exhaust the pressurized air from a pipe 12. The O2 adsobred in the second adsorbing agent is passed through the zone 3 and utilized in the regeneration. Thereby, the O2 concn. in air and the O2 yield ratio can be enhanced to a large extent.