Monoalkyl phosphonic acid ester production process
    3.
    发明授权
    Monoalkyl phosphonic acid ester production process 失效
    单烷基膦酸酯生产工艺

    公开(公告)号:US5554781A

    公开(公告)日:1996-09-10

    申请号:US399253

    申请日:1995-03-06

    IPC分类号: C01B25/24 C07F9/09 C07F9/11

    CPC分类号: C01B25/24 C07F9/09 C07F9/11

    摘要: The invention relates to a process for producing a unique phosphation reagent and to a simple, single-stage process utilizing this reagent to produce alkyl phosphate esters having high monoalkyl phosphate content in combination with low dialkyl phosphate, trialkyl phosphate, phosphoric acid and residual alcohol.

    摘要翻译: 本发明涉及一种独特的磷酸化试剂的制备方法,以及利用该试剂制备具有高烷基磷酸酯含量的磷酸烷基酯与磷酸二烷基酯,磷酸三烷基酯,磷酸和残余醇组合的简单的单步方法。

    In-situ phosphation reagent process
    4.
    发明授权
    In-situ phosphation reagent process 失效
    原位磷酸化试剂工艺

    公开(公告)号:US5550274A

    公开(公告)日:1996-08-27

    申请号:US400077

    申请日:1995-03-07

    IPC分类号: C01B25/24 C07F9/09 C07F9/11

    CPC分类号: C07F9/09 C01B25/24 C07F9/11

    摘要: The invention relates to a simple, single-stage process to produce alkyl phosphate esters having high monoalkyl phosphate content in combination with low dialkyl phosphate, trialkyl phosphate, phosphoric acid and other nonionic (usually residual alcohol) components in which a unique phosphation reagent having a preferred effective equivalent polyphosphoric acid concentration of 121-123% is produced and utilized in-situ.

    摘要翻译: 本发明涉及一种制备具有高磷酸单烷基酯含量的磷酸低烷基酯与磷酸二烷基酯,磷酸三烷基酯,磷酸和其它非离子(通常为残余醇)组分的简单的单步方法,其中独特的磷酸化试剂具有 优选地生产并利用优选的有效等效多聚磷酸浓度为121-123%。

    Process for freeing mineral acids from heavy metals
    5.
    发明授权
    Process for freeing mineral acids from heavy metals 失效
    从重金属中释放无机酸的方法

    公开(公告)号:US4777028A

    公开(公告)日:1988-10-11

    申请号:US009188

    申请日:1987-01-30

    申请人: Klaus Schrodter

    发明人: Klaus Schrodter

    摘要: Mineral acids are freed from heavy metals, especially copper, arsenic, antimony and lead by precipitating the metals in sulfide form. To this end, the mineral acid is reacted with hydrogen sulfide or an alkali metal sulfide solution under pressure and with thorough agitation, and formed solid matter is subsequently separated from the mineral acid under the pressure selected. The mineral acid may conveniently by admixed initially with a filter aid and then treated with hydrogen sulfide or the alkali metal sulfide solution.

    摘要翻译: 矿物酸通过沉淀硫化物形式的金属而从重金属,特别是铜,砷,锑和铅中除去。 为此,无机酸在压力和充分搅拌下与硫化氢或碱金属硫化物溶液反应,随后在所选择的压力下将形成的固体物质与无机酸分离。 无机酸可以方便地通过与助滤剂混合,然后用硫化氢或碱金属硫化物溶液处理。

    Process for the dearsenification of polyphosphoric acid
    7.
    发明授权
    Process for the dearsenification of polyphosphoric acid 失效
    多磷酸脱砷方法

    公开(公告)号:US4399114A

    公开(公告)日:1983-08-16

    申请号:US402941

    申请日:1982-07-29

    IPC分类号: C01B25/24 C01B25/16

    CPC分类号: C01B25/24

    摘要: The disclosure relates to a process for the continuous dearsenification of polyphosphoric acid with the aid of hydrogen sulfide in a gas admission zone. To this end, the disclosure provides for the acid to be dearsenified in a gas admission zone subdivided so as to comprise at least two separate liquid matter-receiving zones, each zone being separated from the other by means of a separate gas zone; for the liquid in each of the liquid matter-receiving zones to be maintained at a level 0.1 up to 10 cm high, without admission of gas; for hydrogen sulfide which remained unreacted in the individual liquid matter-receiving zones to be collected in the respective gas zone and for it to be finely redispersed in the liquid matter-receiving zone directly upstream of the respective gas zone by allowing the hydrogen sulfide to flow through a plurality of openings into the acid, the latter being delivered from the respective liquid-matter-receiving zone into the next downstream liquid-matter-receiving zone, and introduced thereinto directly below the liquid matter level therein; for precipitated arsenic sulfide to be separated from the acid coming from the lower end of the gas admission zone, and for the filtrate obtained to be freed from gaseous hydrogen sulfide in excess.

    摘要翻译: 本公开涉及在气体入口区借助硫化氢连续脱砷多磷酸的方法。 为此,本公开内容提供了在气体进入区域中进行脱砷的酸,其被细分为包括至少两个分离的液体物质接收区域,每个区域通过单独的气体区域与另一个区域分离; 使每个液体物质接收区域中的液体保持在0.1至10厘米高的水平,而不允许气体; 对于在各个液体物质接收区中保持未反应的硫化氢,其被收集在各个气体区中,并且通过允许硫化氢流动直接在各个气体区的上游被精细地再分散在液体物质接收区中 通过多个开口进入酸,后者从相应的液体接收区输送到下一个下游液体接收区,并直接在其中引入液体物质的下方; 使沉淀的硫化砷与气体入口区的下端的酸分离,得到的过滤得到的无水硫化氢的滤液。

    Process utilizing waste material consisting substantially of phosphorous
acid
    8.
    发明授权
    Process utilizing waste material consisting substantially of phosphorous acid 失效
    使用基本上由亚磷酸组成的废料的方法

    公开(公告)号:US3956462A

    公开(公告)日:1976-05-11

    申请号:US451911

    申请日:1974-03-18

    CPC分类号: C01B25/06 C01B25/16

    摘要: Waste material consisting substantially of contaminated phosphorous acid is utilized. To this end, the phosphorous acid is introduced, with agitation into a liquid phase. Liquid phase and phosphorous acid are maintained in a ratio by volume between 1:1 and 10:1. The liquid phase is placed in a reactor, maintained between 250.degree. and 400.degree.C and selected from a phosphoric acid of the general formula H.sub.n.sub.+2 P.sub.n O.sub.3n.sub.+1, in which n substantially stands for a number between 1 and 5. Resulting hydrogen phosphide is removed. In the event of continuous operation, newly formed liquid phase is removed from the reactor, at the same rate as it is being formed.

    摘要翻译: 使用基本上由污染的亚磷酸组成的废料。 为此,在搅拌下将亚磷酸引入液相中。 液相和亚磷酸的体积比保持在1:1至10:1之间。 将液相置于保持在250℃至400℃的反应器中,并选自通式为Hn + 2PnO3n + 1的磷酸,其中n基本上代表1至5之间的数字。产生的磷化氢为 删除。 在连续操作的情况下,新形成的液相以与形成的相同的速率从反应器中除去。

    Concentration of wet-process phosphoric acid
    9.
    发明授权
    Concentration of wet-process phosphoric acid 失效
    湿法处理磷酸的浓度

    公开(公告)号:US3671202A

    公开(公告)日:1972-06-20

    申请号:US3671202D

    申请日:1964-02-21

    申请人: ALLIED CHEM

    IPC分类号: C01B25/24 B01D1/14

    CPC分类号: C01B25/24

    摘要: THIS INVENTION RELATES TO THE CONCENTRATION OF WETPROCESS PHOSPHORIC ACID TO PRODUCE SUPERPHOSPHORIC ACID BY CONTACTING WET-PROCESS PHOSPHORIC ACID, PREFERABLY CONTAINING FROM ABOUT 50-55% P2O5, WITH A STREAM OF HOT COMBUSTION GASES IN SUCH A VOLUME AND AT SUCH A VELOCITY TO SUBSTANTIALLY COMPLETELY ENTRAIN ALL OF THE WETPROCESS PHOSPHORIC ACID, CONTINUOUSLY FEEDING THE STREAM OF HEATING GAS CONTAINING THE ENTRAINED ACID INTO A ZONE WHERE COALESCENCE OF THE ACID PARTICLES IS EFFECTED AND

    CONTINUOUSLY REMOVING THE RESULTING SUPERPHOSPHORIC ACID.