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    • 1. 发明授权
    • Vehicle heat source control device and method for controlling vehicle heat source
    • 车辆热源控制装置及车辆热源控制方法
    • US08612092B2
    • 2013-12-17
    • US13343211
    • 2012-01-04
    • Tsuyoshi OkamotoTsutomu TashiroKeisuke Tani
    • Tsuyoshi OkamotoTsutomu TashiroKeisuke Tani
    • B60H1/00B60H1/03B60H1/14
    • B60H1/00735B60H1/00764B60H1/00899
    • A request heat calculation unit calculates a request heat power requested to heat sources to supply. A heat cost calculation unit calculates a relationship between a heat power supplied from each of the heat sources and a heat cost, which is a fuel quantity consumed to supply a unit heat power. An abnormal source detection unit detects an abnormal heat source, which cannot normally supply a heat power, from the heat sources. An abnormal heat calculation unit calculates an abnormal heat power supplied from the abnormal heat source. A determination unit determines distribution of heat power supplied from the heat sources based on both the relationship and the abnormal heat power, such that a sum of the heat power supplied from the heat sources coincides with the request heat power, and the heat cost of all the heat sources is minimized.
    • 请求热计算单元计算要求供热源的请求热功率。 热成本计算单元计算从每个热源供应的热功率与作为提供单元热功率消耗的燃料量的热成本之间的关系。 异常源检测单元从热源检测不能正常供热的异常热源。 异常热计算单元计算从异常热源供给的异常热功率。 确定单元基于两者的关系和异常热功率来确定从热源供应的热功率的分布,使得从热源供应的热功率的总和与请求热功率一致,并且所有热量的热成本 热源最小化。
    • 5. 发明授权
    • Process for producing p-dichlorobenzene
    • 对二氯苯生产方法
    • US08524957B2
    • 2013-09-03
    • US13125933
    • 2009-10-23
    • Tsuyoshi Okamoto
    • Tsuyoshi Okamoto
    • C07C17/00
    • C07C17/12C07C25/08
    • To provide a novel process for producing p-dichlorobenzene satisfying both of high selectivity of p-dichlorobenzene and high conversion of chlorine at the same time.A process for continuously producing p-dichlorobenzene, which is a process for producing p-dichlorobenzene by a nuclear chlorination reaction of benzene and/or chlorobenzene with chlorine, in the presence of a Lewis acid catalyst and a phenothiazine analogue compound, said process comprising; employing a reactor having a first supply route for continuously supplying a mixed solution of benzene and/or chlorobenzene and a Lewis acid catalyst to a reactor, a second supply route for continuously supplying a mixed solution of benzene and/or chlorobenzene and a phenothiazine analogue compound to the above reactor, and a third supply route for continuously supplying chlorine to the above reactor; and supplying these raw materials for the reaction by opening the above first supply route and third supply route in random order at the initiation of reaction, and then opening the above second supply route.
    • 提供同时满足对二氯苯的高选择性和高氯转化率的对二氯苯的新方法。 一种连续生产对二氯苯的方法,该方法是在路易斯酸催化剂和吩噻嗪类似物化合物的存在下,通过苯和/或氯苯与氯的氯化氯反应制备对二氯苯的方法。 使用具有用于将苯和/或氯苯和路易斯酸催化剂的混合溶液连续供应到反应器的第一供给路径的反应器,用于连续供应苯和/或氯苯和吩噻嗪类似物化合物的混合溶液的第二供应途径 和上述反应器连续供给氯的第三供给路径; 并通过在反应开始时以随机的顺序打开上述第一供给路径和第三供给路径来供给这些反应原料,然后打开上述第二供给路径。
    • 7. 发明申请
    • PROCESS FOR PRODUCING P-DICHLOROBENZENE
    • 生产二氯苯腈的方法
    • US20110207976A1
    • 2011-08-25
    • US13125933
    • 2009-10-23
    • Tsuyoshi Okamoto
    • Tsuyoshi Okamoto
    • C07C17/02C07C17/04
    • C07C17/12C07C25/08
    • To provide a novel process for producing p-dichlorobenzene satisfying both of high selectivity of p-dichlorobenzene and high conversion of chlorine at the same time.A process for continuously producing p-dichlorobenzene, which is a process for producing p-dichlorobenzene by a nuclear chlorination reaction of benzene and/or chlorobenzene with chlorine, in the presence of a Lewis acid catalyst and a phenothiazine analogue compound, said process comprising; employing a reactor having a first supply route for continuously supplying a mixed solution of benzene and/or chlorobenzene and a Lewis acid catalyst to a reactor, a second supply route for continuously supplying a mixed solution of benzene and/or chlorobenzene and a phenothiazine analogue compound to the above reactor, and a third supply route for continuously supplying chlorine to the above reactor; and supplying these raw materials for the reaction by opening the above first supply route and third supply route in random order at the initiation of reaction, and then opening the above second supply route.
    • 提供同时满足对二氯苯的高选择性和高氯转化率的对二氯苯的新方法。 一种连续生产对二氯苯的方法,该方法是在路易斯酸催化剂和吩噻嗪类似物化合物的存在下,通过苯和/或氯苯与氯的氯化氯反应制备对二氯苯的方法。 使用具有用于将苯和/或氯苯和路易斯酸催化剂的混合溶液连续供应到反应器的第一供给路径的反应器,用于连续供应苯和/或氯苯和吩噻嗪类似物化合物的混合溶液的第二供应途径 和上述反应器连续供给氯的第三供给路径; 并通过在反应开始时以随机的顺序打开上述第一供给路径和第三供给路径来供给这些反应原料,然后打开上述第二供给路径。
    • 10. 发明申请
    • Lubricant for water-miscible metal working oil
    • 用于水溶性金属加工油的润滑剂
    • US20070010406A1
    • 2007-01-11
    • US10550028
    • 2004-03-19
    • Tsuyoshi OkamotoTakaichi Imai
    • Tsuyoshi OkamotoTakaichi Imai
    • C10M173/00
    • C10M173/02C10M2209/107C10N2220/021C10N2240/407C10N2240/408
    • The present invention provides a lubricant for water-based metal working oil containing polyether (E) represented by the following general formula (1) and having an HLB of 6.1 to 16.0 and a weight-average molecular weight of 500 to 10,000 R1[{(OCH2CH2CH2CH2)m/(OA1)n}(OA2)p—OH]q  (1) [in the formula, R1 denotes a residue such that at least one hydroxyl group is removed from a compound with a carbon number of 1 to 24 having 1 to 6 hydroxyl group(s); A1 denotes an alkylene group with a carbon number of 2 to 4 except a 1,4-butylene group; A2 denotes an alkylene group with a carbon number of 2 to 4; m denotes an integer of 1 or more having an average of 1 to 120; n and p each denotes an integer of 0, 1 or more such that an average of (n+p) is 1 to 200, and n and p are not simultaneously 0; q denotes an integer of 1 to 6; and {(OCH2CH2CH2CH2)m/(OA1)n} in a case where n is an integer of 1 or more denotes a random bond], and water-based metal working oil containing said lubricant. They are superior in lubricity to steel materials as well as, particularly, lubricity to soft metal such as aluminum, and excellent because of stability on dilution with water and non-separation property.
    • 本发明提供一种含有下述通式(1)所示的聚醚(E),HLB为6.1〜16.0,重均分子量为500〜10,000 <η的水性金属加工油的润滑剂。 line-formula description =“In-line Formulas”end =“lead”?> R <1> {{(OCH 2 CH 2 CH 2 CH 2) (OA 2 )(OA 在式中,R 1表示残基,使得至少一个羟基从具有1至6个羟基的碳数为1至24的化合物中除去; 表示除1,4-亚丁基以外碳原子数为2〜4的亚烷基。 A 2 O表示碳数为2〜4的亚烷基; m表示平均值为1〜120的1以上的整数, n和p各自表示0或1以上的整数,使得(n + p)的平均值为1〜200,n和p不同时为0; q表示1〜6的整数, 和{(OCH 2 CH 2 CH 2 CH 2 CH 2)m / 在n为1以上的整数的情况下,表示随机键]和含有所述润滑剂的水性金属加工油。 它们对钢材具有优异的润滑性,特别是对软质金属如铝的润滑性,并且由于用水稀释和非分离性能的稳定性而优异。