Device making phosphorus by thermal process
    2.
    发明授权
    Device making phosphorus by thermal process 有权
    通过热处理制磷

    公开(公告)号:US08784744B2

    公开(公告)日:2014-07-22

    申请号:US13321987

    申请日:2010-05-27

    CPC classification number: C01B25/01 C01B25/02 F27B19/04 F27D3/16

    Abstract: The present invention discloses an apparatus for thermally refining phosphorus. The apparatus comprises: a melting furnace for melting rock phosphate into melts, including a feed port and a melt outlet; and a reduction-oxidation furnace including a furnace body which gas a melt inlet, a slag outlet, and a fume outlet, and a blow gun, wherein the melt inlet and the melt outlet are in communication with each other and wherein the blow gun has an end inserted into the furnace body. The content of impurities in fumes containing phosphorus pentaoxide is low, and the phosphorus pentaoxide can be easily extracted with a high purity of the phosphorus pentaoxide and at low cost by means of the apparatus for thermally refining phosphorus according to the present invention.

    Abstract translation: 本发明公开了一种用于热精炼磷的装置。 该设备包括:熔融炉,用于将磷酸盐磷酸盐熔化成熔体,包括进料口和熔体出口; 以及还原氧化炉,其包括熔体入口,炉渣出口和烟气出口的气体和吹气枪,其中熔体入口和熔体出口彼此连通,并且其中吹气枪具有 一端插入炉体。 含有五氧化二磷的烟雾中的杂质含量低,五氧化二磷可以用五氧化二磷的高纯度容易地提取,并且通过根据本发明的用于热磷精炼的装置以低成本。

    Reduction-oxidation furnace for making phosphorus by thermal process
    3.
    发明授权
    Reduction-oxidation furnace for making phosphorus by thermal process 有权
    通过热处理制备磷的还原氧化炉

    公开(公告)号:US08741226B2

    公开(公告)日:2014-06-03

    申请号:US13321975

    申请日:2010-05-27

    CPC classification number: F27D3/16 C01B25/01 C01B25/02 C01B25/04 F27B1/10

    Abstract: The present invention discloses a reduction-oxidation furnace for thermally refining phosphorus. The reduction-oxidation furnace comprises a furnace body and a blow gun, wherein the furnace body has a slag outlet, a fume outlet, and a melt inlet for feeding melts formed by melting rock phosphate into the furnace body and wherein the blow gun has an end inserted into the furnace body. The content of impurities in fumes containing phosphorus pentaoxide is low, the phosphorus pentaoxide can be easily extracted with a high purity of the phosphorus pentaoxide and at low cost by means of the reduction-oxidation furnace for thermally refining phosphorus according to the present invention.

    Abstract translation: 本发明公开了一种用于热精炼磷的还原氧化炉。 还原氧化炉包括炉体和吹气枪,其中炉体具有炉渣出口,烟气出口和用于将熔融磷酸盐熔融形成的熔体进料到炉体中的熔体入口,并且其中喷枪具有 端插入炉体。 含有五氧化二磷的烟气中的杂质含量低,五氧化二磷可以用五氧化二磷的高纯度容易地提取,并且通过根据本发明的用于热精炼磷的还原氧化炉以低成本提取。

    PROCESS FOR MANUFACTURING PHOSPHOROUS TRICHLORIDE, PHOSPHOROUS PENTACHLORIDE AND CEMENT
    5.
    发明申请
    PROCESS FOR MANUFACTURING PHOSPHOROUS TRICHLORIDE, PHOSPHOROUS PENTACHLORIDE AND CEMENT 审中-公开
    磷酸三钙,磷酸二氢钙和水泥的制造方法

    公开(公告)号:US20110256040A1

    公开(公告)日:2011-10-20

    申请号:US13139254

    申请日:2009-12-11

    Applicant: Keki H. Gharda

    Inventor: Keki H. Gharda

    CPC classification number: C04B7/60 C01B25/01 C01B25/10 C04B2290/20 Y02P40/123

    Abstract: A process for manufacturing phosphorous trichloride, phosphorous pentachloride and cement comprising of heating at elevated temperature of 1100° C. to 1500° C. pulverised mixture of phosphate ores, carbonaceous substances, silica and/or alumina and treating the resultant gaseous products with chlorine in the ratio of 1 to 5 moles of chlorine per mole of phosphorous oxide contained in the phosphate ores while maintaining the temperature between 400° C. to 1000° C. by cooling and thereafter firstly separating gaseous mixture of primarily phosphorous trichloride and phosphorous pentachloride, from cement and later separating phosphorous trichloride and phosphorous pentachloride, both separations by known methods.

    Abstract translation: 制备三氯化磷,五氯化磷和水泥的方法,其包括在1100℃至1500℃的升高温度下加热磷酸盐矿石,含碳物质,二氧化硅和/或氧化铝的粉碎混合物,并将所得的气态产物用氯处理 通过冷却保持温度在400℃至1000℃之间,然后首先将主要为三氯化磷和五氯化磷的气态混合物从磷酸盐矿石中的每摩尔磷氧化物中的1至5摩尔氯的比例从 水泥,后来分离出三氯化磷和五氯化磷,两种分离方法均采用已知方法。

    Method of filtering phosphate utilizing a rotary table filter or horizontal table filter
    6.
    发明授权
    Method of filtering phosphate utilizing a rotary table filter or horizontal table filter 失效
    使用旋转台式过滤器或水平式过滤器过滤磷酸盐的方法

    公开(公告)号:US07736526B2

    公开(公告)日:2010-06-15

    申请号:US12285415

    申请日:2008-10-03

    CPC classification number: C01B25/01 B01D33/15 B01D33/463 B01D33/60

    Abstract: The present disclosure is directed to a filter support having a surface with a plurality of perforations therein. At least one spray bar may be substantially fixed adjacent to the surface of the filter support. A spray bar may include a plurality of nozzles for directing a pressured fluid toward the filter support. The filter support may further include a motor for causing the filter support to move in a cyclical manner while the spray bar directs pressurized fluid toward the filter support.

    Abstract translation: 本公开涉及一种具有其中具有多个穿孔的表面的过滤器支撑件。 至少一个喷杆可以基本上固定在过滤器支撑件的表面附近。 喷杆可以包括用于将加压流体引向过滤器支撑件的多个喷嘴。 过滤器支撑件还可以包括用于使过滤器支撑件以循环方式移动的电动机,同时喷射杆将加压流体引向过滤器支撑件。

    Preparation of phosphatic feedstock from phosphorus-containing waste
    8.
    发明授权
    Preparation of phosphatic feedstock from phosphorus-containing waste 失效
    从含磷废物制备磷酸盐原料

    公开(公告)号:US6051201A

    公开(公告)日:2000-04-18

    申请号:US106787

    申请日:1998-06-25

    Inventor: James C. Barber

    CPC classification number: C01B25/023 C01B25/01 C01B25/027

    Abstract: Phosphorus furnaces were operated by the Tennessee Valley Authority (TVA) to produce elemental phosphorus beginning over the period 1936-1976. Elemental phosphorus was lost in phosphorus-containing waste throughout the 40 years TVA produced the element. Large quantities of phosphorus-containing wastes remain at the site where TVA produced the chemical.Technology has not been available to treat phosphorus-containing waste so as to recover elemental phosphorus and produce an innocuous waste material. White phosphorus is a dangerous chemical and it is very toxic. Essentially all the elemental phosphorus must be recovered if an innocuous waste is produced. Commercial processes have not been available to recover elemental phosphorus from phosphorus-containing wastes.Elemental phosphorus is produced commercially by smelting phosphatic material in electric furnaces. A process has been invented to prepare phosphatic feedstock from phosphorus-containing waste. The waste is heated in a temperature range which will volatilize white phosphorus and convert white phosphorus into red phosphorus. Thus phosphorus-containing wastes can be safely agglomerated to prepare phosphatic feedstock. Feedstock is heated to approximately 2700.degree. F. in electric furnaces and red phosphorus is vaporized. White phosphorus is obtained when phosphorus vapor is condensed.

    Abstract translation: 磷酸炉由田纳西河谷管理局(TVA)运营,以在1936 - 1976年期间开始生产元素磷。 元年磷在含磷废物中丧失,整个40年来,TVA产生了这一元素。 在TVA生产化学品的场所,大量含磷废物仍然存在。 技术还没有可用于处理含磷废物,以回收元素磷并产生无害废物。 白磷是一种危险的化学物质,毒性很大。 如果产生无害废物,基本上必须回收所有的元素磷。 从磷含量废物中回收元素磷的商业过程尚不可用。 元素磷通过在电炉中熔化磷酸盐材料而商业化生产。 已经发明了一种从含磷废物制备磷酸盐原料的方法。 废物在使白磷挥发并将白磷转化为红磷的温度范围内加热。 因此,含磷废物可以安全地聚集以制备磷酸盐原料。 原料在电炉中加热至约2700°F,红磷蒸发。 当磷蒸气冷凝时,得到白磷。

    Production of phosphorus and phosphoric acid
    10.
    发明授权
    Production of phosphorus and phosphoric acid 失效
    生产磷和磷酸

    公开(公告)号:US4608241A

    公开(公告)日:1986-08-26

    申请号:US728620

    申请日:1985-04-29

    Inventor: James C. Barber

    CPC classification number: C02F1/52 C01B25/01 C01B25/027 C05B17/00

    Abstract: Processes are disclosed for recovering solid wastes containing elemental phosphorus. The wastes may cause serious environmental problems at phosphorus furnaces because elemental phosphorus is toxic to marine animals. Recovery of the wastes was considered for the following.1. At phosphorus furnace plants making phosphoric acid as one of the products, when the objective is to produce only high-quality phosphoric acid.2. At phosphorus furnace plants making elemental phosphorus as a final product, and the objective is to produce only high-quality phosphorus.3. At plant sites where neither phosphoric acid nor phosphorus is produced.The processes include recycling the wastes to phosphorus furnaces. All of the phosphorus acid produced in 1 can be highly concentrated with low impurities content. In 2, all the low-quality phosphorus is recycled to the phosphorus furnaces and all the product is high grade. In 3, phosphorus furnaces are not available at the plant site and recycling the solid wastes is impractical. In this case processes are disclosed for recovering the elemental phosphorus from the waste, converting the residue to granular fertilizer, and making suspension fertilizer from water containing elemental phosphorus.

    Abstract translation: 公开了用于回收含有元素磷的固体废物的方法。 由于元素磷对海洋动物有毒,废弃物可能对磷炉造成严重的环境问题。 以下考虑废物的回收。 在磷化炉厂将磷酸作为产品之一,目的是生产优质磷酸。 2.磷化炉生产元素磷作为最终产品,目的是生产优质磷。 3.在不生产磷酸和磷的植物地点。 这些过程包括将废物回收到磷炉。 1中产生的所有磷酸都可以高度浓缩,杂质含量低。 2,所有低质量的磷被回收到磷炉,所有的产品都是高档的。 3,磷厂在厂址不可用,而且固体废物的再循环是不切实际的。 在这种情况下,公开了用于从废物中回收元素磷的过程,将残余物转化为颗粒肥料,并从含有元素磷的水中制备悬浮肥料。

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