首页> 外国专利> Oil-bearing sands and shales, their mixtures as raw materials for fixing or dissociating carbon dioxide and NOx, and for producing cristalline silicium, hydrogen, silicon nitride, silicium carbide and silanes

Oil-bearing sands and shales, their mixtures as raw materials for fixing or dissociating carbon dioxide and NOx, and for producing cristalline silicium, hydrogen, silicon nitride, silicium carbide and silanes

机译:含油砂岩和页岩及其混合物,用作固定或分解二氧化碳和NOx的原料,并用于生产结晶硅,氢,氮化硅,碳化硅和硅烷

摘要

Preparation of crystalline silicon and hydrogen and production of silicon nitride, silicon carbide, monosilanes and higher silanes using oil-containing sands and/or shales as raw materials, comprises treating the raw materials with the other reactants fluorine and hydrogen; and simultaneously separating the resulting amorphous aluminum fluoride using a floatation method and fine filtration. Preparation of crystalline silicon and hydrogen and production of silicon nitride, silicon carbide, monosilanes and higher silanes using oil-containing sands and/or shales as raw materials, comprises treating the raw materials with the other reactants fluorine and hydrogen, until the resulting very hot hydrogen fluoride transforms the silicate-containing rock into gaseous components such as silicon tetrafluoride and aluminum trifluoride, in order to allow the very hot gaseous silicon tetrafluoride, which is in the form of its salt, such as potassium hexafluorosilicate to react exothermally with aluminum grit to form crystalline silicon in the form of crystal flakes; and simultaneously separating the resulting amorphous aluminum fluoride using a floatation method and fine filtration and the obtained aluminum trifluoride is combined with the originally developed aluminum trifluoride, in order to later be freed of fluorine and re-converted by molten salt electrolysis into metallic aluminum, which itself can be used in the initial process once again, such that the separated crystalline silicon can be purified by zone melting method or can be allowed to directly chemically react with pure cold nitrogen to form silicon nitride while discharging heat, where: instead of the employed nitrogen, carbon resulting from the reaction can be used to produce silicon carbide, which like silicon nitride plays a role in the ceramic industry; the crystalline silicon has to be catalytically refined with hydrogen and/or monosilane to form monosilane or higher silanes, by means of which the mineral oil of the sands, acts as an agent for supplying the primary energy and is pyrolytically dissociated at greater than 100[deg]C largely into hydrogen and a graphite-likes mass, so that it is possible to remove the formed hydrogen of the hydrocarbon chain from the reaction to feed into existing pipeline systems of the natural gas industry, while the crystalline silicon can assume a leading energy-efficient role in the future because at greater than 350[deg] C, the above-mentioned silanes deliver atomic hydrogen, which has a half-life of half a second, and thus producing the strongest reducing chemical substance, while the resulting silicon radicals can be compared with the oxidation of atomic oxygen with respect to the energy capacity, which can be easily observed in atmospheric thunderstorms.
机译:以含油的砂子和/或页岩为原料,制备晶体硅和氢,以及生产氮化硅,碳化硅,甲硅烷和高级硅烷,包括用其他反应物氟和氢处理原料;同时使用浮选法和精细过滤分离得到的无定形氟化铝。使用含油的砂子和/或页岩作为原料制备结晶硅和氢,以及生产氮化硅,碳化硅,甲硅烷和高级硅烷,包括用其他反应物氟和氢处理该原料,直到产生非常热的氟化氢将含硅酸盐的岩石转变成气态组分,例如四氟化硅和三氟化铝,以使呈盐形式的非常热的气态四氟化硅(例如六氟硅酸钾)与铝砂放热反应,从而以晶体薄片的形式形成晶体硅;并同时使用浮选法和精细过滤分离所得的无定形氟化铝,并将所得的三氟化铝与最初开发的三氟化铝混合,以随后除去氟并通过熔融盐电解将其重新转化为金属铝,本身可以再次用于初始工艺中,这样分离出的结晶硅可以通过区域熔化法纯化,或者可以与纯净的冷氮直接化学反应形成氮化硅,同时释放热量,其中:反应产生的氮,碳可用于生产碳化硅,就像氮化硅在陶瓷工业中一样;晶体硅必须用氢和/或甲硅烷进行催化精制,以形成甲硅烷或高级硅烷,借助它们,沙子中的矿物油可作为提供一次能量的试剂,并在大于100的温度下热解离解。 ℃下大部分变成氢气和类石墨团块,因此有可能从反应中除去烃链中形成的氢气,以供入天然气行业现有的管道系统中,而结晶硅可以发挥主导作用由于上述硅烷在高于350℃时会发出原子氢,氢的半衰期为半秒,因此会产生最强的还原性化学物质,而生成的硅则会在未来起到节能作用就能量容量而言,可以将自由基与原子氧的氧化进行比较,这在大气雷暴中很容易观察到。

著录项

  • 公开/公告号EP1857168A3

    专利类型

  • 公开/公告日2011-06-22

    原文格式PDF

  • 申请/专利权人 SINCONO AG;

    申请/专利号EP20060022578

  • 发明设计人 KRASS FLORIAN;

    申请日2006-10-29

  • 分类号B01D53/62;C01B31/36;C01B21/068;C01F7/42;

  • 国家 EP

  • 入库时间 2022-08-21 17:58:48

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