会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 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
    • Process for the preparation of high purity aluminas starting from impure
aluminum chloride solutions
    • 从不纯的氯化铝溶液开始制备高纯度氧化铝的方法
    • US4486402A
    • 1984-12-04
    • US449867
    • 1982-12-15
    • Bernard GurtnerRobert BarralRoland Bachelard
    • Bernard GurtnerRobert BarralRoland Bachelard
    • C01F7/22C01F7/30B01D9/02
    • C01F7/22C01F7/306C01P2004/60C01P2006/12
    • Process for the preparation of high purity alumina containing less than 0.1 weight percent of residual chlorine starting from impure aluminum chloride solutions, which process comprises a crystallization step to provide aluminum chloride hexahydrate crystals having a diameter of from about 400 to about 4000 micrometers in the presence of hydrochloric acid; washing the aluminum chloride hexahydrate crystals so obtained with pure hydrochloric acid; and pyrohydrolyzing the washed crystals of aluminum chloride hexahydrate at a temperature of from about 700.degree. to about 1300.degree. C., in which pyrohydrolysis a gas is forced through a layer of the washed aluminum chloride hexahydrate so as to remove the gaseous reaction products while obviating any possible movement of the solid by the gas, the process particularly producing transition aluminas simultaneously having a specific surface area greater than 100 m.sup.2 /g and a chlorine content less than 0.1 weight percent.
    • 从不纯的氯化铝溶液开始制备含有小于0.1重量%残留氯的高纯度氧化铝的方法,该方法包括结晶步骤,以在存在下提供直径为约400至约4000微米的氯化铝六水合物晶体 的盐酸; 用纯盐酸洗涤得到的氯化铝六水合物晶体; 并在约700℃至约1300℃的温度下将洗涤的氯化铝六水合物热解水解,其中热水解将气体强制通过洗涤的氯化铝六水合物层,以除去气态反应产物,同时消除 通过气体的固体的任何可能的移动,该方法特别地产生同时具有大于100m 2 / g的比表面积和小于0.1wt%的氯含量的过渡氧化铝。
    • 8. 发明授权
    • Process for the production of uranium trioxide having a large specific
surface from hydrated uranyl nitrate
    • 从水合铀酰硝酸盐生产具有大比表面积的三氧化铀的方法
    • US4585634A
    • 1986-04-29
    • US563382
    • 1983-12-05
    • Roland BachelardPierre Lakodey
    • Roland BachelardPierre Lakodey
    • C01G43/01C01G43/06
    • C01G43/066C01G43/01C01P2006/12C01P2006/60C01P2006/80
    • A process for the production of uranium trioxide having a large specific surface by the thermal denitration of hydrated uranyl nitrate corresponding to the formula UO.sub.2 (NO.sub.3).sub.2 .multidot.xH.sub.2 O, in which 2.ltoreq.x.ltoreq.6, characterized in that, in a first stage, the said nitrate is treated in the form of a liquid at room temperature in the range from 160.degree. C. to 260.degree. C. until a solid phase containing at least 55% by weight of uranium is obtained and, in a second stage, the said solid phase is progressively heated to a temperature of at most 600.degree. C. at a heating rate of at most 1000.degree. C. per hour, and is kept at this temperature of at most 600.degree. C. until a second solid phase of UO.sub.3 having a large specific surface is obtained. The UO.sub.3 product produced has a specific surface of at least 10 m..sup.2 g.sup.-1.
    • PCT No.PCT / FR83 / 00083 Sec。 371日期:1983年12月5日 102(e)1983年12月5日日期PCT提交1983年4月29日PCT公布。 出版物WO83 / 03820 日期:1983年11月10日。一种生产具有大比表面积的三氧化铀的方法,该方法是通过对应于式UO2(NO3)2×H2O的水合铀酰硝酸盐进行热脱硝,其中2≤x≤6, 其特征在于,在第一阶段中,所述硝酸盐在室温下在160℃至260℃的范围内以液体的形式进行处理,直至含有至少55重量%铀的固相为 并且在第二阶段中,所述固相以至多1000℃/小时的加热速率逐渐加热至至多600℃的温度,并且保持在该温度至多600℃ 直到获得具有大比表面积的UO 3的第二固相。 所生产的UO3产品的比表面积至少为10m2g-1。