Production of iron (II) chloride and chlorine from ferric chloride
    1.
    发明授权
    Production of iron (II) chloride and chlorine from ferric chloride 失效
    从氯化铁生产氯化铁(II)和氯

    公开(公告)号:US4026999A

    公开(公告)日:1977-05-31

    申请号:US613001

    申请日:1975-09-12

    IPC分类号: C01B7/03 C01G49/10

    CPC分类号: C01G49/10

    摘要: A process is provided for manufacturing iron(II)chloride from iron(III)chloride. Iron(III)chloride is introduced in dimeric form into a reactor or it is vaporized into the dimeric form in the reactor. The dimeric iron(III)chloride vapor rises into the upper part of the reactor where it is completely condensed to the monomeric form. The condensed monomeric iron(III)chloride falls within the reactor to the lower part of the reactor where it is again vaporized. From this reacting circulating system of iron(III)chloride, solid iron(II)chloride is left in the lower part of the reactor. The solid iron(II)chloride is then removed from the reactor.

    摘要翻译: 提供了从氯化铁(III)制造氯化铁(II)的方法。 将氯化铁(III)以二聚体形式引入反应器中,或者在反应器中蒸发成二聚体形式。 氯化二聚铁(III)蒸气上升到反应器的上部,其完全冷凝成单体形式。 冷凝的单体氯化铁(III)在反应器内部落入反应器的下部,再次蒸发。 从氯化铁(III)的这种反应循环系统中,将氯化铁(II)留在反应器的下部。 然后将氯化铁(II)从反应器中取出。

    Producing hydrogen and oxygen by decomposition of water via the
thermochemical iron-chlorine system
    2.
    发明授权
    Producing hydrogen and oxygen by decomposition of water via the thermochemical iron-chlorine system 失效
    通过热化学铁 - 氯系统分解水生产氢气和氧气

    公开(公告)号:US4024230A

    公开(公告)日:1977-05-17

    申请号:US613000

    申请日:1975-09-12

    CPC分类号: C01B3/063 C01B3/105 Y02E60/36

    摘要: Decomposition of water to hydrogen and oxygen with the aid of a thermochemical cyclic process based upon the iron/chlorine system by reduction of FeCl.sub.2 in the presence of H.sub.2 to Fe, oxidation of the Fe with steam to Fe.sub.3 O.sub.4, treatment of the hot Fe.sub.3 O.sub.4 with steam and chlorine to obtain oxygen, conversion of themixture of iron oxides so obtained with hydrogen chloride to FeCl.sub.2 and recycling of the FeCl.sub.2 to the reduction stage, wherein a part of the heat required for the process is supplied by heating the hydrogen and steam in indirect heat exchange with a hot coolant from a high temperature nuclear reactor. The conversion of the iron oxides to FeCl.sub.2 is carried out via the intermediate stage of dimeric FeCl.sub.3 and it is thus possible to convey the solid reaction products by free fall through the reaction zones.

    摘要翻译: 借助于基于铁/氯系统的热化学循环过程,将水分解成氢和氧,通过在H 2存在下将FeCl 2还原成Fe,将Fe用蒸汽氧化成Fe 3 O 4,用蒸汽处理热的Fe 3 O 4 和氯以获得氧气,用氯化氢将如此获得的氧化铁的混合物转化成FeCl 2并将FeCl 2再循环到还原阶段,其中通过以间接加热方式加热氢气和蒸汽来供应该方法所需的一部分热量 与来自高温核反应堆的热的冷却液进行交换。 铁氧化物转化为FeCl 2通过二聚FeCl 3的中间阶段进行,因此可以通过自由落体通过反应区输送固体反应产物。

    Process for obtaining hydrogen and oxygen from water
    3.
    发明授权
    Process for obtaining hydrogen and oxygen from water 失效
    从水中获取氢和氧的方法

    公开(公告)号:US4011305A

    公开(公告)日:1977-03-08

    申请号:US512797

    申请日:1974-10-04

    摘要: A process for the dissociation of water into hydrogen and oxygen in a multi-stage closed cycle process using a system involving at least one metallic element having multiple valency and at least one halogen, characterized in that a halide of the multiple valency metallic element is subjected to a mixture of steam and hydrogen converting the halide to a mixture of the metallic element and at least one oxide thereof, said latter mixture is subjected to steam to produce a mixed valency oxide of the metallic element accompanied by the liberation of hydrogen, and said mixed valency oxide is then subjected to a hydrogen halide to convert it back to the said metallic halide with the liberation of oxygen.

    Process for recycling waste sulfuric acid
    4.
    发明授权
    Process for recycling waste sulfuric acid 失效
    回收废硫酸的方法

    公开(公告)号:US5527985A

    公开(公告)日:1996-06-18

    申请号:US427981

    申请日:1995-04-21

    摘要: A process for recycling waste sulfuric acid by decomposing organic contaminants by use of light energy, comprising exposing a waste sulfuric acid containing contaminants to a focused radiation emission having an irradiation intensity within the range of from 0.01 to 100 MW/m.sup.2 in a reaction chamber shaped as a directly-absorbing receiver, wherein the chamber is maintained at a temperature within the range of from 200.degree. C. to 1000.degree. C. to form sulfur trioxide and water as sulfuric acid decomposition products. The process also includes forming sulfur dioxide and oxygen, starting materials for sulfuric acid, by cleavage of the decomposition product sulfur trioxide by maintaining the reaction chamber at a temperature between 400.degree. C. and 1500.degree. C. The process, particularly adapted for irradiations with direct solar radiation.

    摘要翻译: 一种通过使用光能分解有机污染物来回收废硫酸的方法,包括将含有污染物的废硫酸暴露于具有0.01至100MW / m 2范围内的照射强度的聚焦辐射发射的反应室中形成 作为直接吸收式接收器,其中室保持在200℃至1000℃的温度范围内以形成三氧化硫和水作为硫酸分解产物。 该方法还包括通过将反应室保持在400℃至1500℃之间的温度,通过裂解分解产物三氧化硫来形成二氧化硫和氧气,用于硫酸的原料。该方法特别适用于 直接太阳辐射。