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    • 1. 发明授权
    • Method for deinking
    • 脱墨方法
    • US6077389A
    • 2000-06-20
    • US50802
    • 1998-03-31
    • Minoru SawaiYoichi Ishibashi
    • Minoru SawaiYoichi Ishibashi
    • D21C5/02D21B1/08
    • D21C5/027Y02W30/648
    • A deinking method for obtaining regenerated pulp of high brightness is provided. One or more of deinking agents selected from (a-1) to (a-2) given below are used, and a deinking step is carried out, in which a washing step is carried out at treating temperatures from 40 to 80.degree. C.;(a-1) : a compound represented by the general formula (a-1) given below,R.sub.1 --O--(AO).sub.p --H (a-1)where R.sub.1 is an alkyl group or an alkenyl group having 14 to 24 carbon atoms, AO is specific quantities of EO and PO, and p is a number to satisfy the specific quantities,(a-2): a compound represented by the general formula (a-2) given below,R.sub.2 [--COO--(AO).sub.m --R.sub.3 ].sub.n (a-2)where n is an integer of one or more, R.sub.2 is a residue of carboxylic acid having 14 to 24 carbon atoms in total, R.sub.3 is hydrogen atom or an alkyl group having 1 to 20 carbon atoms and the like, AO is specific quantities of EO and PO, and m is a number to satisfy the specific quantities.
    • 提供了一种用于获得高亮度的再生浆的脱墨方法。 使用选自下述(a-1)〜(a-2)的脱墨剂中的一种以上的脱墨剂,进行在40〜80℃的处理温度下进行洗涤工序的脱墨工序。 ; (a-1):由下式给出的通式(a-1)表示的化合物:R1-O-(AO)pH(a-1)其中R1是烷基或具有14-24个碳原子的烯基 AO是特定量的EO和PO,p是满足特定量的数(a-2):由下列通式(a-2)表示的化合物,R2 [-COO-(AO) m-R3] n(a-2)其中n是一个或多个的整数,R2是总共具有14-24个碳原子的羧酸的残基,R3是氢原子或具有1-20个碳原子的烷基 AO是EO和PO的特定量,m是满足特定量的数。
    • 2. 发明授权
    • Exhaust control valve structure for 2-cycle engine
    • 2循环发动机排气控制阀结构
    • US6095103A
    • 2000-08-01
    • US83666
    • 1998-05-22
    • Yoichi IshibashiMasahiro Asai
    • Yoichi IshibashiMasahiro Asai
    • F01L5/04F01L5/20F02B25/20F02B75/02F02D9/04F02D13/02
    • F02D13/0284F02B2075/025Y02T10/18
    • An exhaust passage for connecting to an exhaust port of a cylinder is provided. The exhaust passage includes a first path extending in a direction generally orthogonal to the central axis of the exhaust port. A second path connects the first path and the exhaust poil and a control valve is provided in the first path. The rotational axis of the exhaust control valve is generally parallel to the direction in which the first path extends. The surface area of an opening connecting the first path and the second path is variable as the exhaust control valve rotates, so as to carry out controlled combustion and exhaust timing. This makes it unnecessary to provide a hollow section for housing an exhaust control valve and bearing at a position close to the exhaust. It is also possible to reduce the size of a cylinder block and to realize smooth flow of exhaust gases by making the inner peripheral surface of the exhaust passage smooth.
    • 设置有用于连接到气缸的排气口的排气通道。 排气通道包括沿与排气口的中心轴线大致正交的方向延伸的第一路径。 第二路径连接第一路径和排气歧管,并且在第一路径中设置有控制阀。 排气控制阀的旋转轴线大致平行于第一路径延伸的方向。 连接第一路径和第二路径的开口的表面积随着排气控制阀旋转而变化,以便执行受控的燃烧和排气定时。 这使得不需要在靠近排气的位置设置用于容纳排气控制阀和轴承的中空部分。 也可以通过使排气通路的内周面平滑地减小气缸体的尺寸,实现废气的平稳流动。
    • 4. 发明授权
    • Combustion controller for a spark ignition type two-cycle engine
    • 用于火花点火式双冲程发动机的燃烧控制器
    • US5697332A
    • 1997-12-16
    • US633519
    • 1996-04-17
    • Masahiro AsaiYoichi IshibashiShinichi IsomuraOsamu KudoKenji Nishida
    • Masahiro AsaiYoichi IshibashiShinichi IsomuraOsamu KudoKenji Nishida
    • F02B1/04F02B1/12F02B75/02F02D13/02F02D41/30F02B9/00F02B11/00F02B25/20
    • F02D13/0284F02B75/02F02D41/3035F02B1/04F02B1/12F02B2075/025F02D2400/04Y02T10/18
    • A combustion controller for a two-cycle engine which enables to cause self firing always at the optimum timing is provided. The combustion controller comprises an exhaust control valve 15 provided in the vicinity of an exhaust port 7 of the two-cycle engine 1 and capable of fully closing the exhaust port and driving control means 47, 38, 39, 40 and 37 to drive the exhaust control valve 15 according to a control map giving an exhaust opening ratio .theta..sub.e depending at least on the engine speed and the throttle valve opening ratio .theta..sub.th in order to control the pressure in the cylinder during up-stroke of the piston 8. The exhaust control valve 15 is formed by a thin shell-like member comprising an exhaust control portion 35 substantially along the cylinder curvature in the exhaust port 7 and wider than the whole width of the exhaust port and a swinging arm portion 34 for connecting at least a side of the exhaust control portion and the rotational shaft 33 perpendicular to the cylinder axis and accommodated in a receiving recess formed in the cylinder block. This receiving recess is communicated with the exhaust passage extending from the exhaust port 7 only in the working zone of the exhaust control portion.
    • 提供了一种能够始终在最佳定时引起自发火的用于双冲程发动机的燃烧控制器。 燃烧控制器包括设置在两冲程发动机1的排气口7附近并能够完全关闭排气口和驱动控制装置47,38,39,40和37以驱动排气的排气控制阀15 控制阀15根据控制图给出排气开度比θe,该排气开度比θe至少取决于发动机转速和节气门开度比θth,以便在活塞8的上行程中控制气缸中的压力。排气 控制阀15由包括排气控制部分35的薄壳体构成,该排气控制部分35基本上沿着排气口7中的气缸曲率并且宽于排气口的整个宽度;以及摆臂部分34,用于至少连接一侧 排气控制部分和旋转轴33垂直于气缸轴线并且容纳在形成在气缸体中的容纳凹部中。 该收纳凹部与仅在排气控制部的工作区域从排气口7延伸的排气通路连通。
    • 5. 发明授权
    • Deinking method
    • 脱墨方法
    • US5302243A
    • 1994-04-12
    • US880087
    • 1992-05-05
    • Yoichi IshibashiYoshinao KonoYoshitaka MiyauchiTakanobu ShiroishiHiromichi Takahashi
    • Yoichi IshibashiYoshinao KonoYoshitaka MiyauchiTakanobu ShiroishiHiromichi Takahashi
    • D21C5/02
    • D21C5/027Y02W30/648
    • The present invention aims at developing a deinking method applicable to the deinking of, for example, waste OA (office automation) paper and telephone directories, whereby a deinked pulp having a high whiteness and little contamination with large ink spots and unliberated ink can be obtained. The object of the present invention can be achieved by deinking, for example, waste OA paper or telephone directories by using a deinking composition containing as an effective component a reaction mixture (III) obtained by conducting the addition reaction of ethylene oxide and propylene oxide with a mixture (I) comprising a fat and oil (a) and a mono- to hexahydric alcohol (b) and/or with a transesterification mixture (II) obtained by conducting the transesterification reaction of a fat and oil (a) with a mono- to hexahydric alcohol (b), in such a manner that the molar ratio of ethylene oxide to propylene oxide which are used as starting materials ranges from 0.8 to 1.2 and that the molar number of ethylene oxide which is used for the addition reaction ranges from 50 to 100 mol per mole of the fat and oil (a).
    • 本发明旨在开发适用于例如废弃OA(办公室自动化)纸和电话簿的脱墨的脱墨方法,由此可以获得具有高白度和少量污染的脱墨纸浆,并且可以获得大的墨点和未起泡的油墨 。 本发明的目的可以通过使用含有作为有效成分的脱墨组合物来脱墨,例如废纸OA或电话簿,通过进行环氧乙烷和环氧丙烷的加成反应获得的反应混合物(III) 包含脂肪和油(a)和一至六元醇(b)的混合物(I)和/或通过脂肪和油(a)与单体(a)进行酯交换反应而获得的酯交换混合物(II) - 以六元醇(b)的形式,使用作为原料的环氧乙烷与环氧丙烷的摩尔比为0.8〜1.2,加成反应所用的环氧乙烷的摩尔数为 每摩尔脂肪和油(a)为50-100摩尔。
    • 6. 发明申请
    • DEVICE FOR PRODUCING ETHANOL AND METHOD FOR PRODUCING ETHANOL
    • 用于生产乙醇的装置和用于生产乙醇的方法
    • US20130175158A1
    • 2013-07-11
    • US13809269
    • 2011-07-21
    • Takafumi KiuchiRyohta HidakaYoichi IshibashiTomonori SumiYasuhiko KatohYasuki KanshaAtsushi Tsutsumi
    • Takafumi KiuchiRyohta HidakaYoichi IshibashiTomonori SumiYasuhiko KatohYasuki KanshaAtsushi Tsutsumi
    • B01D3/14
    • B01D3/143C12M21/12C12M47/10C12P7/06C12P7/10Y02E50/16Y02E50/17
    • Disclosed are a method for producing ethanol and a device for producing ethanol that are suitable to the recycled use of an enzyme.The device is configured from: a vacuum distillation tower (11) into which an ethanol-fermented liquid generated by saccharification fermentation of a biomass starting material is introduced, and with the interior in a state that is at a lower pressure than atmospheric pressure, that subjects the ethanol-fermented liquid to distillation, distilling ethanol vapor that contains water vapor, and removing as a bottom product the enzyme-containing concentrated waste liquid that is roused for saccharification fermentation of the biomass starting material; and a fractionating tower (12) for fractionating the ethanol vapor distilled from the vacuum distillation tower (11). In this case, the energy of the ethanol vapor can be more efficiently taken advantage of if the device is provided with a first compressor (16) that adiabatically compresses the ethanol vapor distilled from the vacuum distillation tower (11), and the ethanol vapor adiabatically compressed by the first compressor (16) is introduced into the fractionating tower (12).
    • 公开了一种生产乙醇的方法和一种适用于再循环使用酶的乙醇生产装置。 该装置由以下部件构成:真空蒸馏塔(11),其中引入通过生物质原料的糖化发酵产生的乙醇发酵液体,并且内部处于比大气压力低的压力的状态,该蒸馏塔 将乙醇发酵液进行蒸馏,蒸馏含有水蒸汽的乙醇蒸汽,并将作为底部产物除去用于生物质原料糖化发酵的含酶浓缩废液; 和用于分馏从真空蒸馏塔(11)蒸馏的乙醇蒸汽的分馏塔(12)。 在这种情况下,如果该装置设置有绝热压缩从真空蒸馏塔(11)蒸馏出的乙醇蒸汽的绝热压缩机(16),并且绝热的乙醇蒸气可以更有效地利用乙醇蒸气的能量 由第一压缩机(16)压缩的气体被引入分馏塔(12)。
    • 9. 发明授权
    • Deinking composition
    • 脱墨组合
    • US5282928A
    • 1994-02-01
    • US889962
    • 1992-05-29
    • Hiromichi TakahashiYoichi IshibashiYoshitaka MiyauchiTakanobu ShiroishiYoshinao Kono
    • Hiromichi TakahashiYoichi IshibashiYoshitaka MiyauchiTakanobu ShiroishiYoshinao Kono
    • C11C3/06D21C5/02
    • C11C3/06D21C5/027Y02W30/648
    • A deinking composition which shows a good deinking performance, a good defoaming property and excellent operation characteristics whereby a deinked pulp having a high whiteness and little contamination with the total remaining ink can be obtained in the reclamation of waste papers by flotation, washing or a combination procedure thereof and wherein the deinking composition comprises a reaction mixture (II), as a deinking agent, obtained by the addition reaction of alkylene oxide (D) with a mixture (I) comprising a fat and oil (A) which is constituted with a mixture of higher fatty acids (a) comprising fatty acids having 8 to 24 carbon atoms; having an average carbon atom number of from 12.7 to 22.5; containing from 9.6 to 70.6% by weight of higher fatty acids having 20 to 24 carbon atoms and having an iodine value (IV) of 70 or less and glycerol (b-1), and/or, a transesterification reaction mixture (B) obtained by reacting the fat and oil (A) with glycerol (b-2), and at least one mono- to tetradecahydric alcohol (C).
    • 脱墨剂组合物具有良好的脱墨性能,良好的消泡性能和优异的操作特性,可以通过浮选,洗涤或组合来回收废纸,从而获得具有高白度和总剩余油墨污染少的脱墨纸浆 其脱墨组合物包含作为脱墨剂的反应混合物(II),其通过环氧烷(D)与包含脂肪和油(A)的混合物(I)的加成反应获得,所述混合物(I)由 含有碳原子数为8〜24的脂肪酸的高级脂肪酸(a)的混合物; 平均碳原子数为12.7〜22.5; 含有9.6〜70.6重量%的具有20〜24个碳原子且碘值(IV)为70以下的高级脂肪酸和甘油(b-1),和/或得到的酯交换反应混合物(B) 通过使脂肪和油(A)与甘油(b-2)和至少一种一至十四元醇(C)反应。
    • 10. 发明授权
    • Ethanol/water vapor permeation membrane separation process with heat and energy recovery via temperature and flow control
    • 乙醇/水蒸汽渗透膜分离过程,通过温度和流量控制进行热能和能量回收
    • US09321011B2
    • 2016-04-26
    • US13809445
    • 2011-07-29
    • Takafumi KiuchiRyohta HidakaYoichi IshibashiYasuki KanshaAtsushi Tsutsumi
    • Takafumi KiuchiRyohta HidakaYoichi IshibashiYasuki KanshaAtsushi Tsutsumi
    • B01D61/36
    • B01D61/362B01D61/368B01D2313/24B01D2313/246B01D2313/38
    • [Problem] To provide a membrane separation apparatus and a membrane separation method capable of reducing energy consumption,[Solution] A membrane separation apparatus (10) includes: a membrane separator (20) supplied with a fluid (X) containing a component (A) and a component (B) and separating the fluid (X) into a fluid (Y) having a higher concentration of the component (A) than the fluid (X) and a fluid (Z) having a lower concentration of the component (A) than the fluid (X) by using a separation membrane; a first compressor (21) adiabatically compressing the fluid (Y); a first heat exchanger (11) to which the fluid (Y) adiabatically compressed by the first compressor (21) is introduced as a heat source; and a second heat exchanger (12) to which the fluid (Z) is introduced as a heat source. The fluid (X) is divided and conveyed by first and second supply lines (31, 32), the divided fluids (X) are heated by the first and second heat exchangers (11, 12), respectively, then merged and supplied to the membrane separator (20).
    • 提供一种能够降低能量消耗的膜分离装置和膜分离方法[方案]一种膜分离装置(10),包括:膜分离器(20),其供给含有成分(A )和组分(B),并且将流体(X)分离成具有比流体(X)更高浓度的组分(A)的流体(Y)和具有较低浓度组分的流体(Z)( A)比流体(X)使用分离膜; 绝热压缩流体(Y)的第一压缩机(21); 引入由第一压缩机(21)绝热压缩的流体(Y)作为热源的第一热交换器(11) 和引入流体(Z)作为热源的第二热交换器(12)。 流体(X)由第一和第二供应管线(31,32)分开并输送,分流体(X)分别被第一和第二热交换器(11,12)加热,然后合并并供应到 膜分离器(20)。