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    • 103. 发明授权
    • Apparatus for distilling shale oil from oil shale
    • 从油页岩中蒸馏页岩油的装置
    • US4431483A
    • 1984-02-14
    • US361579
    • 1982-03-24
    • Takeyoshi ShishidoYoshio Sato
    • Takeyoshi ShishidoYoshio Sato
    • C10B53/06C10B1/04C10G1/02C10B49/06
    • C10B1/04C10G1/02
    • An apparatus for distilling shale oil from oil shale, which comprises: a vertical type distilling furnace which is divided by two vertical partitions each provided with a plurality of vent apertures into an oil shale treating chamber and two gas chambers, said oil shale treating chamber being located between said two gas chambers in said vertical type distilling furnace, said vertical type distilling furnace being further divided by at least one horizontal partition into an oil shale distilling chamber in the lower part thereof and at least one oil shale preheating chamber in the upper part thereof, said oil shale distilling chamber and said oil shale preheating chamber communicating with each other through a gap provided at an end of said horizontal partition, an oil shale supplied continuously from an oil shale supply port provided in said oil shale treating chamber at the top thereof into said oil shale treating chamber continuously moving from the oil shale preheating chamber to the oil shale distilling chamber, a high-temperature gas blown into an oil shale distilling chamber passing horizontally through said oil shale in said oil shale treating chamber, thereby said oil shale is preheated in said oil shale preheating chamber, and a gaseous shale oil is distilled from said preheated oil shale in said oil shale distilling chamber; and a separator for separating by liquefaction a gaseous shale oil from a gas containing the gaseous shale oil discharged from the oil shale preheating chamber.
    • 一种用于从油页岩蒸馏页岩油的装置,包括:垂直式蒸馏炉,其由两个垂直隔板分隔,每个分隔壁设有多个通风孔,分别设置在油页岩处理室和两个气室中,所述油页岩处理室为 位于所述垂直式蒸馏炉中的所述两个气室之间,所述垂直式蒸馏炉进一步由至少一个水平隔板分隔成其下部的油页岩蒸馏室和在上部的至少一个油页岩预热室 所述油页岩蒸馏室和所述油页岩预热室通过设置在所述水平隔板的端部处的间隙相互连通,从位于所述油页岩处理室中的油页岩供应口连续供应的油页岩 将其从油页岩预热室继续移动到所述油页岩处理室中 e油页岩蒸馏室,吹入油页岩蒸馏室的高温气体,水平通过所述油页岩处理室中的所述油页岩,由此所述油页岩在所述油页岩预热室中预热,并且气态页岩油为 在所述油页岩蒸馏室中从所述预热的油页岩蒸馏出来; 以及用于通过液化气体页岩油从含有从油页岩预热室排出的气态页岩油的气体分离的分离器。
    • 105. 发明授权
    • Method for continuously manufacturing high-temperature reducing gas
    • 连续生产高温还原气的方法
    • US4268412A
    • 1981-05-19
    • US91561
    • 1979-11-05
    • Tsuneo MiyashitaYoshio SatoYoshitsugu Ando
    • Tsuneo MiyashitaYoshio SatoYoshitsugu Ando
    • C01B3/42C21B13/00C10K3/06C01B2/22
    • C21B13/0073Y02P10/136Y02P10/212
    • A method for continuously manufacturing a high-temperature reducing gas, comprising: using a reducing gas manufacturing equipment including a heat medium heating apparatus and a gas reforming apparatus provided below said heat medium heating apparatus; burning a fuel gas in said heat medium heating apparatus to continuously produce a high-temperature combustion exhaust gas; on the other hand, introducing heat medium particles having an average particle size within the range of from 50 to 500 .mu.m into said heat medium heating apparatus to heat to a prescribed temperature and fluidize said particles through heat exchange with said high-temperature combustion exhaust gas; blowing a gas to be reformed containing CO.sub.2 and H.sub.2 O and a hydrocarbon-containing gas into said gas reforming apparatus, while introducing said heated and fluidized particles from said heat medium heating apparatus into said gas reforming apparatus; thereby heating said gas to be reformed and said hydrocarbon-containing gas, through heat exchange with said heated and fluidized particles, in said gas reforming apparatus to reform by reaction said gas to be reformed and said hydrocarbon-containing gas into a high temperature reducing gas rich in H.sub.2 and CO; and then, feeding said fluidized particles cooled through said heat exchange with said gas to be reformed and said hydrocarbon-containing gas back into said heat medium heating apparatus, thereby continuously manufacturing a high-temperature reducing gas while using said fluidized particles in recycle.
    • 一种用于连续制造高温还原气体的方法,包括:使用包括设置在所述热介质加热装置下方的热介质加热装置和气体重整装置的还原气体制造设备; 在所述热介质加热装置中燃烧燃料气体以连续地产生高温燃烧废气; 另一方面,将平均粒度为50〜500μm的热介质颗粒引入所述热介质加热装置中以加热到规定温度,并通过与所述高温燃烧排气的热交换使所述颗粒流化 加油站; 将所述加热流化颗粒从所述热介质加热装置引入所述气体重整装置中,将含有CO 2和H 2 O的重整气体和含烃气体吹入所述气体重整装置; 从而通过与所述加热和流化的颗粒的热交换在所述气体重整装置中对所述待重整气体和所述含烃气体进行加热,以使所述待重整气体和所述含烃气体反应成为高温还原气体 富含H2和CO; 然后将通过所述热交换冷却的所述流化颗粒与要重整的气体一起进料,并将所述含烃气体返回到所述热介质加热装置中,由此在循环使用所述流化颗粒的同时连续制造高温还原气体。
    • 107. 发明授权
    • Method of starting up turbines
    • 启动涡轮机的方法
    • US4121424A
    • 1978-10-24
    • US768754
    • 1977-02-15
    • Yoshio SatoMistuyo Nishikawa
    • Yoshio SatoMistuyo Nishikawa
    • F01D17/24F01D19/00F01D19/02F01D25/20F01K13/02
    • F01D19/02F01D25/20F01K13/02F05D2200/11
    • At the point of time to when the turbine speed has come up to a first speed N.sub.1, a thermal stress expected in the turbine when the speed is increased to a second speed N.sub.2 at a rate .alpha..sub.1 is presumed. Thermal stress .sigma..sub.s(t) -.sigma..sub.sT1 at the point of time t.sub.o1 for commencing acceleration to the second speed N.sub.2 is then obtained, which point of time t.sub.o1 would never cause the maximum value of the presumed thermal stress to exceed a predetermined limit .sigma..sub.sl of the thermal stress when the turbine speed is increased at that rate. Then, a length of time T.sub.w1, referred to as a warming time, is determined which is required for the thermal stress .sigma..sub.s(t) to decrease to the level of (.sigma..sub.s(t) -.sigma..sub.sT1) when the warming is continued after the point of time t.sub.o. Subsequently, a length of time (N.sub.2 -N.sub.1)/.alpha..sub.1 required for increasing the turbine speed from N.sub.1 to N.sub.2 at the rate .alpha..sub.1 is calculated. The sum of the warming time T.sub.w and the time (N.sub.2 - N.sub.1)/.alpha..sub.1 required for acceleration is calculated. The lengths of time for starting T.sub.1, T.sub.2, T.sub.3 are found for each of the acceleration rates .alpha..sub.1, .alpha..sub.2, .alpha..sub.3 in speed. The acceleration of the turbine is commenced at the time and with the rate which in combination provide the smallest sum T of time.
    • 在涡轮机速度达到第一速度N1的时间点,假定当速度以速率α1增加到第二速度N2时在涡轮机中预期的热应力。 然后获得在开始加速到第二速度N2的时间点-1处的热应力σs(t) - sigma sT1,哪个时间点to1将永远不会导致推定的热应力的最大值超过预定的极限西格玛 当涡轮机速度以该速率增加时,热应力为sl。 然后,确定当加热继续时,热应力σs(t)降低到(sigma s(t)-σsT1)的水平所需的时间长度Tw1(称为加温时间) 之后的时间到了。 随后,计算以α1的速率将涡轮机速度从N1增加到N2所需的时间长度(N2-N1)/α1。 计算加热时间Tw与加速所需的时间(N2-N1)/α1的和。 对于加速率α1,α2,α3的速度,求出T1,T2,T3开始的时间长度。 涡轮机的加速度在当时开始,并且速度与组合提供最小的时间总和T。