首页> 外国专利> Vanadyl hydrate and vanadium carbide prepn. - by vanadate ion redn., solvent extn. and stripping to form vanadyl hydrate ppte., then reacting with carbon to form carbide

Vanadyl hydrate and vanadium carbide prepn. - by vanadate ion redn., solvent extn. and stripping to form vanadyl hydrate ppte., then reacting with carbon to form carbide

机译:水合氧钒和碳化钒制备。 -通过钒酸盐离子的还原,溶剂的萃取。汽提形成水合氧钒ppte。,然后与碳反应形成碳化物

摘要

Vanadyl hydrate is produced by (a) adding sulphur dioxide and a non-oxidising acid to an aq. soln. of vanadate ions to reduce vanadate to vanadyl ions; (b) extracting vanadyl ions with an organic solvent; (c) stripping the solvent to form a vanadyl hydrate ppte.; and (d) sepg. the ppte. Vanadium carbide is produced by the further steps of (e) mixing the ppte. with carbon; and (f) treating the mixt. in a furnace to form vanadium carbide. The starting soln. is pref. a leach soln. contg. Na metavanadate. In step (a), pref. gaseous SO2 and sulphuric acid are added to give a pH of 1-3 (esp. 2) or an electrochemical potential of -150 to -300 (esp. -200)mV. In a batch process, the SO2 is added first but, in a continuous process, SO2 and sulphuric acid can be added together. In step (b), extn. is pref. carried out in a counter-current manner in at least two stages, pref. with sulphuric acid addn. After the first stage to give pH 1.5-3.5 (pref. 2.5-3), pref. using a 10 vol.% soln. of di-2-ethylhexyl phosphoric acid in a 3 vol.% isodecanol/87 vol.% kerosene solvent. In step (c), vanadyl ions are pref. stripped with NH4OH to form VO(OH)2.xH2O. The resulting organic phase, aq. phase and ppte. are sepd. e.g. in a decanter-concentrater, the ppte. (which does not form an emulsion) being filtered off. The moist filter cake can then be mixed with carbon, pelletised, dried in the absence of oxygen or air and then heated in vacuo or in an inert atmos. to produce V2C.
机译:通过(a)向水溶液中加入二氧化硫和非氧化性酸来生产水合氧钒。 soln。钒酸盐离子以将钒酸盐还原为钒酸盐离子; (b)用有机溶剂萃取钒离子; (c)汽提溶剂以形成水合氧钒。和(d)sepg。 ppte。碳化钒是通过(e)混合ppte的进一步步骤生产的。含碳(f)处理混合物。在熔炉中形成碳化钒。起始溶液。是首选。浸出液续偏钒酸钠。在步骤(a)中,优选。加入气态SO 2和硫酸以使pH为1-3(特别是2)或电化学势为-150至-300(特别是-200)mV。在间歇过程中,首先要添加SO2,但在连续过程中,可以将SO2和硫酸一起添加。在步骤(b)中,分机。是首选。至少在两个阶段以逆流方式进行。与硫酸添加剂。在第一阶段达到pH 1.5-3.5(优选2.5-3)之后,优选。使用10%(体积)的soln。在3%(体积)的异癸醇/ 87%(体积)的煤油溶剂中加入二-2-乙基己基磷酸。在步骤(c)中,优选钒离子。用NH 4 OH汽提形成VO(OH)2·xH 2O。所得有机相,水溶液。相和ppte。是sepd。例如在倾析器浓缩器中,ppte。 (不会形成乳液)被滤出。然后可以将潮湿的滤饼与碳混合,造粒,在没有氧气或空气的情况下干燥,然后在真空或惰性气氛中加热。产生V2C。

著录项

  • 公开/公告号FR2472537A1

    专利类型

  • 公开/公告日1981-07-03

    原文格式PDF

  • 申请/专利权人 UNION CARBIDE CORP;

    申请/专利号FR19800026798

  • 发明设计人 HARRY E. GARDNER;

    申请日1980-12-17

  • 分类号C01B31/30;C01G31/00;

  • 国家 FR

  • 入库时间 2022-08-22 15:02:19

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