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    • 5. 发明授权
    • Extractive distillation method
    • 萃取蒸馏法
    • US4447318A
    • 1984-05-08
    • US479725
    • 1983-03-28
    • Shunichiro OguraMasafumi Miyamoto
    • Shunichiro OguraMasafumi Miyamoto
    • B01D3/40C07C1/00C07C7/08C07C7/10C07C9/00C07C11/00C07C67/00C10G7/08C10G21/20B01D3/00C10G7/00
    • C10G7/08
    • In a method for separating a hydrocarbon mixture into relatively difficultly soluble hydrocarbons and relatively easily soluble hydrocarbons by extractive distillation using a polar solvent comprising feeding the starting hydrocarbon mixture to at least two evaporators, an extractive distillation column, a stripping column and a rectifying column; the improvement wherein(1) the polar solvent discharged at a high temperature from the bottom of the stripping column is recycled to the extractive distillation column after it has been cooled to a suitable temperature by giving up heat to a reboiler of the extractive distillation column, a reboiler of the rectifying column and successively to the two or more evaporators, and(2) the starting hydrocarbon mixture is divided into two or more streams and heated in two or more evaporators, one stream being evaporated in a first evaporator to a pressure necessary for introduction into the extractive distillation column and then fed to the extractive distillation column, and the other stream, after evaporation in a second and subsequent evaporators, being pressurized to a pressure required for introduction into the extractive distillation column by means of a compressor and then fed into the extractive distillation column.
    • 在通过使用极性溶剂的萃取蒸馏将烃混合物分离成相对难溶的烃和相对容易溶解的烃的方法,包括将起始烃混合物进料至至少两个蒸发器,萃取蒸馏塔,汽提塔和精馏塔; 改进之处在于,(1)从汽提塔底部高温排出的极性溶剂在通过向提取蒸馏塔的再沸器放热后将其冷却至合适的温度后再循环到萃取蒸馏塔中, 精馏塔的再沸器并依次连接到两个或更多个蒸发器,和(2)起始烃混合物被分成两个或更多个物流并在两个或更多个蒸发器中加热,一个物流在第一蒸发器中被蒸发成必需的压力 用于引入萃取蒸馏塔中,然后进料到萃取蒸馏塔,另一个流在第二个和随后的蒸发器中蒸发后,通过压缩机被加压至引入萃取蒸馏塔所需的压力,然后 进料到萃取蒸馏塔中。
    • 6. 发明授权
    • Amusement facility, container for amusement facility and installation method of amusement equipment
    • 娱乐设施,娱乐设施用集装箱及娱乐设备的安装方法
    • US06470630B1
    • 2002-10-29
    • US09586085
    • 2000-06-02
    • Masafumi Miyamoto
    • Masafumi Miyamoto
    • E04H100
    • E04B1/34807E04H3/10
    • Amusement equipment can be easily installed in a building at low cost. Also, desired amusement equipment can be renewed easily and at low cost. In a building, an amusement facility is provided by installing a container provided therein with amusement equipment. The building is formed with an opening portion for carrying-in-and-out the container therethrough. A container supporting portion for permitting carrying-in-and-out the container is provided in the building. Accordingly, the container is placed on the container supporting portion through the opening portion to install the amusement equipment in the building. Also, by replacing the container in the building, the amusement equipment can be replaced.
    • 娱乐设备可以轻松地以低成本安装在建筑物中。 此外,所需的娱乐设备可以容易地和低成本地更新。 在建筑物中,通过在其中设置设置有娱乐设备的容器来提供娱乐设施。 该建筑物形成有用于通过其携带和取出容器的开口部分。 在建筑物中设置有用于允许携带和取出容器的容器支撑部分。 因此,通过开口部将容器放置在容器支撑部上,将游乐设备安装在建筑物内。 此外,通过更换建筑物中的容器,可以更换游乐设备。
    • 8. 发明授权
    • Porous particles and cosmetics
    • 多孔颗粒和化妆品
    • US08574600B2
    • 2013-11-05
    • US10544678
    • 2004-02-03
    • Masafumi Miyamoto
    • Masafumi Miyamoto
    • A61K9/00
    • A61K8/8111A61K8/0204A61K8/11A61K2800/412A61Q19/00
    • The invention provides porous particles, a process for producing the porous particles, and cosmetics comprising the porous particles. The porous particles of the invention have an average particle diameter of 75 μm or less, based on polyethylene resin having a crystallization degree of 70% or more. The porous particles further comprise an active ingredient. The process for producing the porous particles, comprises mixing polyethylene resin having a crystallization degree of 70% or more, and a low-molecular weight compound having a melting point lower than the softening temperature (or melting point) of the polyethylene resin, with each other at a temperature not lower than the softening temperature (or melting point) of the polyethylene resin, then spraying the mixture into a gaseous phase or a solvent at a temperature at which the viscosity of the mixture becomes 600 mPa·s or less, and removing the low-molecular weight compound from the resulting particles.
    • 本发明提供多孔颗粒,多孔颗粒的制造方法和包含多孔颗粒的化妆品。 本发明的多孔质粒的结晶度为70%以上的聚乙烯树脂的平均粒径为75μm以下。 多孔颗粒还包含活性成分。 制造多孔颗粒的方法包括混合结晶度为70%以上的聚乙烯树脂和熔点低于聚乙烯树脂的软化温度(或熔点)的低分子量化合物, 另外在不低于聚乙烯树脂的软化温度(或熔点)的温度下,在混合物的粘度为600mPa·s以下的温度下将混合物喷入气相或溶剂中, 从所得颗粒中除去低分子量化合物。
    • 10. 发明申请
    • PROCESS FOR PRODUCING NON-CRYSTALLINE CELLULOSE
    • 生产非晶体纤维素的方法
    • US20120103324A1
    • 2012-05-03
    • US13321330
    • 2010-05-19
    • Kazutomo OsakiKeiichiro TomiokaNaoki NojiriMasahiro UmeharaMasafumi Miyamoto
    • Kazutomo OsakiKeiichiro TomiokaNaoki NojiriMasahiro UmeharaMasafumi Miyamoto
    • C08B1/00
    • A61K8/731A61Q19/00C08B1/00C08B1/06C08B15/08
    • The invention relates to a highly productive process for producing decrystallized cellulose which includes treating a cellulose-containing raw material by means of a mill, wherein the cellulose-containing raw material has a cellulose content of a residue obtained by removing water from the cellulose-containing raw material of 20 mass % or more, has a cellulose I-type crystallinity of cellulose more than 33% as calculated from the following formula (1): Cellulose I-type Crystallinity (%)=[(I22.6−I18.5)/I22.6]×100  (1), wherein I22.6 is a diffraction intensity of a lattice plane (002 plane) as measured at a diffraction angle 2θ of 22.6° in X-ray diffraction analysis; and I18.5 is a diffraction intensity of an amorphous moiety as measured at a diffraction angle 2θ of 18.5° in X-ray diffraction analysis, and has a water content of 1.8 mass % or less, to thereby reduce the cellulose I-type crystallinity to 33% or less.
    • 本发明涉及生产非晶纤维素的高效生产方法,其包括用研磨机处理含纤维素的原料,其中含纤维素的原料具有通过从含纤维素的水中除去水而获得的残留物的纤维素含量 原料为20质量%以上,纤维素I型结晶度(%)= [(I22.6〜I18.5)],纤维素I型结晶度为33%以上 )/ I22.6]×100(1),其中I22.6是在衍射角2θ处测量的晶格面(002平面)的衍射强度; 在X射线衍射分析中为22.6°; I18.5是在衍射角2θ处测量的非晶部分的衍射强度; 的X射线衍射分析中为18.5°,水含量为1.8质量%以下,从而将纤维素I型结晶度降低至33%以下。