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    • 63. 发明授权
    • Optical multiplexer/demultiplexer and waveguide type optical coupler
    • 光复用器/解复用器和波导型光耦合器
    • US06741772B2
    • 2004-05-25
    • US10126311
    • 2002-04-22
    • Satoshi Ide
    • Satoshi Ide
    • G02B634
    • G02B6/12011G02B6/12014G02B6/12016
    • An optical multiplexer/demultiplexer that the passband characteristic of demultiplexed optical signal in a waveguide on the output side can be controlled accurately. Long and narrow guide waveguides, being areas where an effective refractive index is greater than an effective refractive index of a sector slab waveguide on the input side, are formed in the core or in an area adjacent to the core so that the long and narrow guide waveguides will branch at the center of curvature of the sector slab waveguide and so that the long and narrow guide waveguides will extend in an output direction without intersecting with one another. When optical signal is input to the sector slab waveguide, the light is guided more strongly through areas where the guide waveguides are formed. As a result, with the propagation of the optical signal, a peak corresponding to the shape of the guide waveguides will appear in the shape of a mode of the optical signal. Therefore, the shape of a mode of optical signal which propagates can be controlled accurately according to a passband characteristic needed in an optical output waveguide.
    • 可以精确地控制输出侧波导中的解复用光信号的通带特性的光复用器/解复用器。 在芯或与芯相邻的区域中形成有长且窄的导向波导,其中有效折射率大于输入侧的扇形板波导的有效折射率的区域,使得长而窄的导向 波导将在扇形平板波导的曲率中心处分支,使得长而窄的导波导将在输出方向上延伸而不相互交叉。 当光信号被输入到扇形平板波导时,光被更强地引导通过形成导向波导的区域。 结果,随着光信号的传播,对应于导波导形状的峰将以光信号的形式出现。 因此,可以根据光输出波导所需的通带特性,精确地控制传播的光信号的形状。
    • 64. 发明授权
    • Signal amplifying circuit connected to a transfer circuit having a known non-linear transfer characteristic
    • 连接到具有已知非线性传输特性的传输电路的信号放大电路
    • US06292058B1
    • 2001-09-18
    • US09360461
    • 1999-07-23
    • Satoshi IdeKohei Shibata
    • Satoshi IdeKohei Shibata
    • H03G320
    • H03K5/082
    • In a signal amplifying circuit connected to a transfer circuit having a known non-linear transfer characteristic and a transient characteristic, a threshold generation circuit generates a threshold signal based on an input signal, a threshold control circuit controls the threshold signal so as to correct the non-linear transfer characteristic of the transfer circuit provided at a former stage based on the input signal. Also, basic amplifying circuit blocks can be connected in a multistage form, each of which is composed of a threshold generation circuit and a differential amplifying circuit, and control the threshold signal of a latter stage block so as to correct the non-linear transfer characteristic of a basic amplifying circuit block at a former stage based on the input signal. In addition, basic amplifying circuit blocks can be connected in a multistage form, each of which includes a peak master-slave threshold generation circuit or a bottom master-slave threshold generation circuit, and control the threshold signal of the differential amplifying circuit of each circuit block.
    • 在连接到具有已知非线性传输特性和瞬态特性的传输电路的信号放大电路中,阈值产生电路基于输入信号产生阈值信号,阈值控制电路控制阈值信号,以校正 基于输入信号在前一级设置的传送电路的非线性传输特性。 此外,基本放大电路块可以以多级形式连接,每个形式由阈值产生电路和差分放大电路组成,并且控制后级块的阈值信号,以便校正非线性传输特性 基于输入信号的前级的基本放大电路块。 此外,基本放大电路块可以以多级形式连接,每个形式包括峰值主从阈值生成电路或底部主从阈值生成电路,并且控制每个电路的差分放大电路的阈值信号 块。
    • 65. 发明授权
    • Process for transferring liquefied gases between containers
    • 在容器之间转移液化气体的过程
    • US06237348B1
    • 2001-05-29
    • US09341571
    • 1999-07-14
    • Satoshi IdeMasayoshi ImotoTakashi Shibanuma
    • Satoshi IdeMasayoshi ImotoTakashi Shibanuma
    • F17C702
    • F17C7/02F17C5/02
    • A liquefied gas is transfer filled by drawing out a nonazeotropic mixture stored in a first container and containing at least two liquefied gases differing in boiling point as essential components from a liquid phase thereof. The mixture is then transferred filled into a second container. The first container is filled with a supplement liquid or supplement gas in an amount making up for the portion of the capacity of the first container that is equal to the decrease in volume of the liquid phase of the nonazeotropic mixture resulting from transfer filling. The supplement liquid is the liquid phase of the liquefied gas mixture having the same composition as that of the nonazeotropic mixture stored in the first container. The supplement gas is a gaseous phase of a liquefied gas mixture having the same composition as that of the nonazeotropic mixture stored in the first container or a gaseous phase composed of at least one component of the nonazeotropic mixture and containing the component having the lowest boiling point of all of the components of the mixture in a proportion larger than the proportion in the nonazeotropic mixture. Alternatively, the supplement gas may be a compressed gas.
    • 通过抽出存储在第一容器中的非共沸混合物并且将至少两种沸点不同的液化气体作为必要组分从其液相中进行转移来填充液化气体。 然后将混合物充填到第二容器中。 第一容器充满补充液体或补充气体,其量为第一容器的容量部分的量,其等于由转移填充物引起的非共沸混合物的液相的体积减小。 补充液体是具有与储存在第一容器中的非共沸混合物相同组成的液化气体混合物的液相。 补充气体是液体气体混合物的气相,其具有与存储在第一容器中的非共沸混合物相同的组成或由非共沸混合物的至少一种组分组成的气相,并且含有具有最低沸点的组分 的混合物的所有组分的比例大于非共沸混合物中的比例。 或者,补充气体可以是压缩气体。
    • 66. 发明授权
    • Process for producing phenolic resin foams
    • 生产酚醛树脂泡沫的方法
    • US6133332A
    • 2000-10-17
    • US341300
    • 1999-07-08
    • Satoshi IdeTakashi Shibanuma
    • Satoshi IdeTakashi Shibanuma
    • C08J9/14C08K5/02C08L61/06C08L61/10
    • C08J9/149C08J2203/14C08J2203/142C08J2361/00C08J2361/04
    • This invention discloses a process for producing a phenolic resin foam, the process comprising the step of reacting a liquid phenolic resin with an acidic curing agent in the presence of a low-boiling organic compound-based blowing agent, the process being characterized in that the low-boiling organic compound-based blowing agent is a mixed blowing agent comprising 1,1,1,3,3-pentafluoropropane and at least one of a hydrocarbon having a boiling point in the range of 40 to 80.degree. C. and a hydrogen-containing fluorohydrocarbon having a boiling point in the range of 40 to 80.degree. C., the proportion of the mixed blowing agent being 5 to 20% by weight based on the liquid phenolic resin.The process is capable of giving high heat insulation property, flame retardancy and in situ applicability to the phenolic resin foam.
    • PCT No.PCT / JP97 / 04759 Sec。 371日期:1999年7月8日 102(e)日期1999年7月8日PCT 1997年12月22日PCT公布。 公开号WO98 / 30623 日期1998年7月16日本发明公开了一种生产酚醛树脂发泡体的方法,该方法包括在低沸点有机化合物基发泡剂存在下使液体酚醛树脂与酸性固化剂反应的步骤, 其特征在于,低沸点有机化合物类发泡剂是包含1,1,1,3,3-五氟丙烷和沸点在40〜80℃的烃中的至少一种的混合发泡剂 C和沸点为40〜80℃的含氢氟代烃,混合发泡剂的比例为5〜20重量%,基于液体酚醛树脂。 该方法能够赋予酚醛树脂泡沫高的隔热性,阻燃性和原位适用性。
    • 67. 发明授权
    • Method for charging refrigerant blend
    • 制冷剂混合物的充气方法
    • US6058717A
    • 2000-05-09
    • US117103
    • 1998-10-13
    • Satoshi IdeTakashi Shibanuma
    • Satoshi IdeTakashi Shibanuma
    • F25B1/00C09K5/04F25B45/00F25B41/00
    • C09K5/045C09K2205/22C09K2205/34
    • The present invention provides a method for charging a refrigerant blend characterized in that, in case of employing as refrigerant a non-azeotropic blend comprising 23% by weight of difluoromethane, 25% by weight of pentafluoroethane and 52% of 1,1,1,2-tetrafluoroethane, composition change associated with transfer is allow to fall within the permissible range of performance of the non-azeotropic refrigerant blend by adjusting a composition of the non-azeotropic blend in a feeding container such as bomb to 23.5-25.0% by weight of difluoromethane, 23.5-25.0% by weight of pentafluoroethane and 50.0-53.0% by weight of 1,1,1,2-tetrafluoroethane followed by discharging the non-azeotropic blend from a liquid phase at 40.degree. C. or less. According to the charging method, composition change associated with transfer of non-azeotropic HFC32/HFC125/HFC134a refrigerant blend may be allowed to fall within the permissible range of performance of refrigerant.
    • PCT No.PCT / JP97 / 04298 Sec。 371日期:1998年10月13日 102(e)日期1998年10月13日PCT 1997年11月25日PCT公布。 公开号WO98 / 23703 日本1998年6月4日本发明提供了一种装载制冷剂共混物的方法,其特征在于,在使用作为制冷剂的情况下,包含23重量%的二氟甲烷,25重量%的五氟乙烷和52重量%的1 ,1,1,2-四氟乙烷,与转移相关的组成变化允许通过将饲料容器(例如炸弹)中的非共沸混合物的组成调节至23.5(以下),从而落入非共沸混合制冷剂共混物的允许的性能范围内 -25.0重量%的二氟甲烷,23.5-25.0重量%的五氟乙烷和50.0-53.0重量%的1,1,1,2-四氟乙烷,随后在40℃从液相中排出非共沸混合物。 或更少。 根据装料方法,可能允许与非共沸HFC32 / HFC125 / HFC134a制冷剂共混物转移相关的组成变化落在制冷剂性能允许范围内。