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    • 81. 发明授权
    • Atmospheres for heat treating non-ferrous metals and alloys
    • 用于热处理有色金属和合金的气氛
    • US5298090A
    • 1994-03-29
    • US995617
    • 1992-12-22
    • Diwakar GargBrian B. BonnerDonald P. EichelbergerKerry R. Berger
    • Diwakar GargBrian B. BonnerDonald P. EichelbergerKerry R. Berger
    • C21D1/76F27D7/06F27D23/00C21D1/00
    • F27D7/06C21D1/763
    • A process for producing low-cost atmospheres suitable for annealing, brazing, and sintering non-ferrous metals and alloys from non-cryogenically produced nitrogen containing up to 5%, residual oxygen is disclosed. According to the process, suitable atmospheres are produced by 1) pre-heating the non-cryogenically produced nitrogen stream containing residual oxygen to a desired temperature, 2) mixing it with more than a stoichiometric amount a hydrocarbon gas, 3) passing it through a reactor packed with a platinum group of metal catalyst to reduce the residual oxygen to very low levels and convert it to a mixture of moisture and carbon dioxide, and 4) using the reactor effluent stream for annealing, brazing, and sintering non-ferrous metals and alloys in a furnace. The key features of the disclosed process include 1) pre-heating the non-cryogenically produced nitrogen containing residual oxygen to a certain minimum temperature, 2) adding more than a stoichiometric amount of a hydrocarbon gas to the pre-heated nitrogen stream, and 3) using a platinum group of metal catalyst to initiate and sustain the reaction between oxygen and the hydrocarbon gas.
    • 公开了一种用于生产低成本气氛的方法,该方法适用于从含低至5%残留氧的非低温法生产的氮中退火,钎焊和烧结有色金属和合金。 根据该方法,通过以下方式产生合适的气氛:1)将含有残余氧气的非低温生成氮气流预热至所需温度,2)将其与多于化学计量的烃气体混合,3)将其通过 反应器用铂族金属催化剂填充,将残余氧气降低至非常低的水平,并将其转化为水分和二氧化碳的混合物,以及4)使用反应器流出物流进行退火,钎焊和烧结有色金属, 合金在炉中。 所公开的方法的主要特征包括:1)将非低温法生产的含氮残留氧预加热到一定的最低温度; 2)向预热的氮气流中加入多于化学计量的烃类气体; 3) )使用铂族金属催化剂引发和维持氧气和烃气体之间的反应。
    • 82. 发明授权
    • Integrated process for producing atmospheres suitable for heat treating
from non-cryogenically generated nitrogen
    • 用于生产适合于从非低温生成的氮进行热处理的气氛的综合方法
    • US5284526A
    • 1994-02-08
    • US995625
    • 1992-12-22
    • Diwakar GargBrian B. BonnerDonald P. Eichelberger
    • Diwakar GargBrian B. BonnerDonald P. Eichelberger
    • B01D53/46B01D53/86C21D1/76F27B9/04F27D19/00C21D11/00F27D23/00
    • F27D19/00B01D53/46B01D53/8671C21D1/763F27B9/045
    • An integrated two-step process for producing low-cost atmospheres suitable for annealing ferrous and non-ferrous metals and alloys, brazing metals, sealing glass to metals, and sintering metal and ceramic powders in continuous furnaces from non-cryogenically produced nitrogen containing up to 3% residual oxygen is disclosed. The residual oxygen present in non-cryogenically produced nitrogen is converted to moisture by mixing it hydrogen and passing the mixture through a reactor packed with a platinum group catalyst in the first step of the process. The reactor effluent stream containing a mixture of nitrogen, unreacted hydrogen, and moisture is mixed with a predetermined amount of a hydrocarbon gas and introduced into the heating zone of a continuous furnace in the second step of the process to 1) convert moisture to a mixture of carbon monoxide and hydrogen by reaction with the hydrocarbon gas via water gas shift reaction and 2) produce atmospheres in-situ suitable for heat treating. The key features of the process include 1) use of economical amount of hydrogen to convert residual oxygen to moisture in an external catalytic reactor and 2) conversion of moisture to a mixture of carbon monoxide and hydrogen by reaction with the hydrocarbon gas via water gas shift reaction in the hot zone of a continuous furnace. The disclosed process is particularly suitable for producing low-cost heat treating atmospheres for continuous furnaces operated at 700.degree. C. and above.
    • 一种用于生产低成本气氛的综合两步法,适用于退火黑色金属和有色金属及合金,钎焊金属,密封玻璃与金属,以及烧结金属和陶瓷粉末的连续炉,由非低温法生产的氮气 公开了3%的残余氧。 存在于非低温法生产的氮气中的残留氧气通过在其第一步骤中混合氢气并使混合物通过填充有铂族催化剂的反应器而转化为水分。 将含有氮气,未反应的氢气和水分的混合物的反应器流出物流与预定量的烃气体混合并在该方法的第二步骤中引入连续炉的加热区域,以将水分转化为混合物 的一氧化碳和氢气,通过水煤气变换反应与烃气反应,2)原位产生适合于热处理的气氛。 该方法的主要特征包括:1)使用经济数量的氢气将外部催化反应器中的残余氧转化为水分; 2)通过水煤气转移与碳氢化合物气体反应,将水分转化为一氧化碳和氢气的混合物 在连续炉的热区反应。 所公开的方法特别适用于在700摄氏度及以上的连续炉中生产低成本的热处理环境。
    • 87. 发明授权
    • Hydroconversion of heavy oils
    • 重油加氢转化
    • US4606809A
    • 1986-08-19
    • US750623
    • 1985-07-01
    • Diwakar Garg
    • Diwakar Garg
    • C10G65/10
    • C10G65/10
    • High yields of desired distillate oil are obtained by subjecting heavy oil to catalytic conversion with hydrogen at superatmospheric pressure in a temperature staged process, wherein the oil-catalyst slurry is subjected in the initial stage to a temperature in the range of 780.degree.-825.degree. F. (415.degree.-440.degree. C.) and in a subsequent stage to a temperature which is at least 20.degree. F. higher than that employed in the previous stage, preferably in the range of 800.degree.-860.degree. F. (.about.425.degree.-460.degree. C.).
    • 所需的馏出油的高产率是通过在温度分级方法中使重油与氢气在超大气压下进行催化转化而获得的,其中油催化剂浆料在初始阶段进行到780-825℃的温度 (415°-440℃),并在随后的阶段中升温至比上一级高至少20°F的温度,优选在800°-860°F的范围内。(差异 425°-460℃)。