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PROCESS DESIGN AND PRODUCTION OF BORON TRICHLORIDE FROM NATIVE BORON CARBIDE IN LAB-SCALE

机译:实验室规模从天然碳化硼中制备三氧化钛的工艺设计和生产

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Turkiye owns the biggest boron mine reserves of the world, so it is a necessity to research the possibilities of obtaining high-tech products of boron. This study is oriented to provide one of two main inputs, boron trichloride (BCl_3) gas and carbon/tungsten core, for production of boron fiber manufactured by well-hidden hot filament CVD method.In this study, the production of BCl_3 from native boron carbide (B_4C) was aimed. In the production process, two different originally designed set-ups were used. In the set-ups, the reaction occurred by passing chlorine gas (Cl_2) through B4C layer (10-110 g) which has different heap heights. The reactor was a vertical quartz tube heated up to 850 °C by a tube furnace with silicon carbide (SiC) heating element. Chlorine as reaction gas and nitrogen as purging gas were dried in two different columns with calcium chloride (CaCl_2) and molecular sieve package. Flow rates of Cl_2, pressure and temperature changes in the set-ups were controlled respectively by rotameter, mass-flow controller (MFC), mercury U-tube manometer, thermocouple and thermometers which were placed in different zones. The product gases were separated in consecutive distillation columns and waste gases were conveyed to a rashing ring packaged gas scrubber. In pipelines, traps and condensers, various melal (i.e. Fe, Al, W, Si, and Cr) halides depending on the impurities of B_4C were detected in different phases. The products in form of gas, liquid and solid were analyzed with FTIR, AAS, XRD and SEM/EDS. Production efficiencies (up to 85 %) and consumption rate of Cl_2 (up to 91 %) were assigned.
机译:Turkiye拥有世界上最大的硼矿储量,因此有必要研究获得硼高科技产品的可能性。这项研究的目的是提供两种主要的输入量之一,即三氯化硼(BCl_3)气体和碳/钨芯,用于通过隐蔽的热丝CVD方法生产硼纤维。 在这项研究中,目标是从天然碳化硼(B_4C)生产BCl_3。在生产过程中,使用了两个不同的最初设计的装置。在装置中,通过使氯气(Cl_2)穿过堆高不同的B4C层(10-110 g)而发生反应。该反应器是一个垂直的石英管,该管由带有碳化硅(SiC)加热元件的管式炉加热到850°C。在两个不同的色谱柱中,分别用氯化钙(CaCl_2)和分子筛包装干燥氯气(作为反应气体)和氮气(作为吹扫气体)。分别通过转子流量计,质量流量控制器(MFC),汞U形管压力计,热电偶和温度计分别控制Cl_2的流量,压力和温度变化,并将它们置于不同的区域。在连续的蒸馏塔中分离出产物气体,并将废气输送到装有鼓环的气体洗涤塔中。在管道,疏水阀和冷凝器中,在不同相中检测到取决于B_4C杂质的各种金属卤化物(即Fe,Al,W,Si和Cr)。用FTIR,AAS,XRD和SEM / EDS分析了气体,液体和固体形式的产物。分配了生产效率(高达85%)和Cl_2的消耗率(高达91%)。

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