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    • 2. 发明授权
    • Metal carbide and nitride powders
    • 金属碳化物和氮化物粉末
    • US4851203A
    • 1989-07-25
    • US30210
    • 1987-03-25
    • Roland BachelardPhilippe Joubert
    • Roland BachelardPhilippe Joubert
    • C01B21/06C01B21/064C01B21/068C01B21/072C01B21/076C01B31/30
    • B82Y30/00C01B21/06C01B21/0685C01B21/0726C01B31/30C01B21/064C01B21/076C01P2002/04C01P2002/60C01P2004/50C01P2004/61C01P2004/64C01P2006/12C01P2006/14C01P2006/80
    • Metal carbide and metal nitride powders produced by the carbothermal reduction of one or more metal oxides reacted with a binder material and a carbonaceous additive or optionally, a binder capable of supplying carbon to the reaction. The metal oxides are selected from among SiO.sub.2, Al.sub.2 O.sub.3, TiO.sub.2, ZrO.sub.2, HfO.sub.2 and B.sub.2 O.sub.3 and are combined with the binder in the presence of carbon to form granules having a controlled pore volume. The granules are then subjected to a carbothermal reduction reaction, in the presence of a nitrogen or a neutral atmosphere, to produce metal nitrides or metal carbides respectively, having an excess of carbon incorporated therein. The product is subsequently heated to react the excess carbon within the compound with oxygen from the atmosphere to form carbon monoxide gas, which may be removed by an optional exhaust system. The remaining metal carbide or metal nitride powder may then be collected and used in various applications such as the production of ceramic objects.
    • 通过一种或多种金属氧化物的碳热还原生产的金属碳化物和金属氮化物粉末与粘合剂材料和碳质添加剂反应,或任选地,能够向反应供应碳的粘合剂。 金属氧化物选自SiO 2,Al 2 O 3,TiO 2,ZrO 2,HfO 2和B 2 O 3,并且在碳存在下与粘合剂组合以形成具有受控孔体积的颗粒。 然后,在氮气或中性气氛的存在下,将颗粒进行碳热还原反应,分别制备其中含有过量碳的金属氮化物或金属碳化物。 随后将产物加热以使化合物中的多余碳与来自大气的氧气反应以形成一氧化碳气体,其可通过可选的排气系统除去。 然后可以收集剩余的金属碳化物或金属氮化物粉末并用于各种应用中,例如制造陶瓷物体。
    • 3. 发明授权
    • Method of making metal carbide and nitride powders
    • 制造金属碳化物和氮化物粉末的方法
    • US4784839A
    • 1988-11-15
    • US30405
    • 1987-03-25
    • Roland BachelardPhilippe Joubert
    • Roland BachelardPhilippe Joubert
    • C01B21/06C01B21/064C01B21/068C01B21/072C01B21/076C01B31/30C01B31/36
    • B82Y30/00C01B21/06C01B21/0685C01B21/0726C01B31/30C01B21/064C01B21/076C01P2002/04C01P2002/60C01P2004/50C01P2004/61C01P2004/64C01P2006/12C01P2006/14C01P2006/80
    • Metal carbide and metal nitride powders produced by the carbothermal reduction of one or more metal oxides reacted with a binder material and a carbonaceous additive or optionally, a binder capable of supplying carbon to the reaction. The metal oxides are selected from among SiO.sub.2, Al.sub.2 O.sub.3, TiO.sub.2, ZrO.sub.2, HfO.sub.2 and B.sub.2 O.sub.3 and are combined with the binder in the presence of carbon to form granules having a controlled pore volume. The granules are then subjected to a carbothermal reduction reaction, in the presence of a nitrogen or a neutral atmosphere, to produce metal nitrides or metal carbides respectively, having an excess of carbon incorporated therein. The product is subsequently heated to react the excess carbon within the compound with oxygen from the atmosphere to form carbon monoxide gas, which may be removed by an optional exhaust system. The remaining metal carbide or metal nitride powder may then be collected and used in various applications such as the production of ceramic objects.
    • 通过一种或多种金属氧化物的碳热还原生产的金属碳化物和金属氮化物粉末与粘合剂材料和碳质添加剂反应,或任选地,能够向反应供应碳的粘合剂。 金属氧化物选自SiO 2,Al 2 O 3,TiO 2,ZrO 2,HfO 2和B 2 O 3,并且在碳存在下与粘合剂组合以形成具有受控孔体积的颗粒。 然后,在氮气或中性气氛的存在下,将颗粒进行碳热还原反应,分别制备其中含有过量碳的金属氮化物或金属碳化物。 随后将产物加热以使化合物中的多余碳与来自大气的氧气反应以形成一氧化碳气体,其可通过可选的排气系统除去。 然后可以收集剩余的金属碳化物或金属氮化物粉末并用于各种应用中,例如制造陶瓷物体。
    • 6. 发明授权
    • Removal of sulfate ions from saline solutions comprised thereof
    • 从其组成的盐溶液中除去硫酸根离子
    • US5536415A
    • 1996-07-16
    • US319224
    • 1994-10-06
    • Philippe Joubert
    • Philippe Joubert
    • C01G25/00B01J20/06C01D3/16C25B15/08B01D15/00
    • C01D3/16
    • Contaminating amounts of sulfate ions are removed from aqueous saline solutions comprised thereof by (i) contacting such saline solution with a zirconium compound, at an acidic pH, (ii) separating the resulting medium into (a) a saline solution depleted in sulfate ions and (b) a zirconium compound onto which said sulfate ions are sorbed, (iii) desorbing the sulfate ions from the stage (ii) zirconium compound at a basic pH, and (iv) separating the medium of desorption into (1) a basic aqueous solution enriched in sulfate ions and (2) a zirconium compound substantially devoid of sulfate ions, with the proviso that the zirconium compound is a novel hydrated zirconium hydroxide having the formula Zr(OH).sub.4 .multidot.xH.sub.2 O, in which x ranges from 4 to 200, and such zirconium compound comprising an undried gelatinous precipitate thereof.
    • (i)在酸性pH下使这种盐溶液与锆化合物接触,(ii)将得到的培养基分离成(a)贫去硫酸根离子的盐水溶液和 (b)在其上吸附所述硫酸根离子的锆化合物,(iii)在碱性pH下从阶段(ii)锆化合物解吸硫酸根离子,和(iv)将解吸介质分离成(1)碱性水溶液 富含硫酸根离子的溶液和(2)基本上不含硫酸根离子的锆化合物,条件是锆化合物是具有式Zr(OH)4×H 2 O的新型水合氢氧化锆,其中x为4至200,以及 这种锆化合物包含未干燥的凝胶状沉淀物。
    • 8. 发明授权
    • Data processing machine network architecture
    • 数据处理机网络架构
    • US6101616A
    • 2000-08-08
    • US887254
    • 1997-07-02
    • Philippe JoubertThierry LeconteBruno Rochat
    • Philippe JoubertThierry LeconteBruno Rochat
    • H04L29/06H04L29/08H04L29/12G06F11/16G06F15/16
    • H04L29/12018H04L29/12839H04L61/10H04L61/6022H04L67/1002H04L67/1008
    • The invention relates to data processing machine network architecture and more particularly relates to the load balancing of data servers. A data server (3) is constituted by at least two server data processing machines (1, 2) capable of providing the same services. The server data processing machines (1, 2) have the same physical address MAC0 to which the same network protocol address is assigned in order to establish connections of client machines to the server (3), which is considered as a single virtual machine. Each server data processing machine comprises filtering means so that each connection of a client machine (5, 6, 7, 8, 9, 10) to the virtual machine corresponds to a unique connection effective with one and only one server data processing machine (1 or 2). The filtering means of each server data processing machine (1, 2) take into account at least one indicator of the status of each server data processing machine (1, 2) having the same physical address MAC0.
    • 本发明涉及数据处理机网络架构,更具体地涉及数据服务器的负载平衡。 数据服务器(3)由能够提供相同服务的至少两个服务器数据处理机(1,2)构成。 服务器数据处理机器(1,2)具有与其分配相同网络协议地址的相同的物理地址MAC0,以便建立客户端机器与被认为是单个虚拟机的服务器(3)的连接。 每个服务器数据处理机包括过滤装置,使得客户端机器(5,6,7,8,9,10)到虚拟机的每个连接对应于与一个且仅一个服务器数据处理机器(1)有效的唯一连接 或2)。 每个服务器数据处理机(1,2)的过滤装置考虑到具有相同物理地址MAC0的每个服务器数据处理机(1,2)的状态的至少一个指示符。
    • 10. 发明授权
    • Process for the selective separation of uranium, zirconium and/or
hafnium and/or molybdenum from a carbonated aqueous solution containing
same
    • 从含有它们的碳酸水溶液中选择性分离铀,锆和/或铪和/或钼的方法
    • US4675166A
    • 1987-06-23
    • US660893
    • 1984-10-15
    • Philippe Joubert
    • Philippe Joubert
    • C22B60/02C01G43/00
    • C22B60/0278
    • Process for the selective separation of uranium in carbonated aqueous solution from soluble impurities including in particular at least one of the elements zirconium and/or hafnium and/or molybdenum, thereby making it possible to produce a uraniferous liquor in a greatly improved state of purity, comprising precipitation of the zirconium and/or hafnium by introducing an alkali metal hydroxide, then separation of the zirconiferous precipitate which possibly contains hafnium and/or molybdenum from the resulting uraniferous solution with its reduced impurities content, which still possibly contains molybdenum, which is characterized in that in order to increase the removal of zirconium and/or hafnium and/or molybdenum, the uraniferous carbonated aqueous solution is treated by means of a dilute alkaline aqueous solution containing at most 17 g/l of at least one alkali metal hydroxide expressed in respect of OH.sup.-, in an amount such that the resulting pH-value is imperatively higher than 11 but is generally between 11.8 and 12.5.
    • 在碳酸水溶液中从可溶性杂质(特别是至少一种元素锆和/或铪和/或钼)中选择性分离铀的方法,从而使得可以以极大地改善的纯度状态生产尿素液体, 包括通过引入碱金属氢氧化物沉淀锆和/或铪,然后从其所含的含铀溶液中分离可能含有铪和/或钼的含锆沉淀物,其还含有可能含有钼的杂质含量,其特征在于 因为为了增加锆和/或铪和/或钼的去除,通过含有至多17g / l的至少一种碱金属氢氧化物的稀碱性水溶液处理含尿碳酸水溶液 OH-的含量,使得所得pH值必须高于11b ut通常在11.8和12.5之间。