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    • 2. 发明授权
    • Submergible fish cage
    • 潜水鱼笼
    • US5299530A
    • 1994-04-05
    • US917853
    • 1992-07-17
    • Hasham MukadamJohn W. Morgan
    • Hasham MukadamJohn W. Morgan
    • A01K61/00A01K63/00A01K61/02
    • A01K61/007
    • A submergible fish cage comprising: a float; a fish cage; at least one (1) anchor weight; and at least one (1) cable, one end of the cable attached to the float element, a middle portion of the cable attached to the fish cage, the bottom end of the cable attached to the anchor element, the cable being shorter than the depth of the water in which the submergible fish cage is placed; the float having a trim tank adapted to be flooded with water, the trim tank adapted to be blown free of water with air, the float element having a minimum of buoyancy sufficient to float itself supporting the fish cage and cable when the trim tank is flooded with water, the float element having a maximum of buoyancy sufficient to float itself supporting the fish cage, anchor weight and cable when the trim tank is charged with air; and the anchor weight having sufficient weight to submerge the float, cage, cable and anchor weight when the trim tank is flooded with water.
    • 一种潜水鱼笼,包括:浮子; 鱼笼 至少一(1)个锚重; 以及至少一个(1)电缆,电缆的一端连接到浮动元件,电缆的中间部分连接到鱼笼,电缆的底端附接到锚固元件,电缆短于 潜水鱼笼放置的水深; 浮子具有适于被水淹没的修整槽,修整槽适于用空气吹出水,浮子元件具有最小的浮力,足以在装饰箱被淹没时浮起来支撑鱼笼和缆索 使用水时,浮动元件具有最大浮力,足以在装饰箱充满空气时自身浮起来支撑鱼笼,锚重物和电缆; 并且锚定重量具有足够的重量以在调整箱被水充满时浸没浮子,保持架,电缆和锚重。
    • 6. 发明授权
    • Removal of magnesium and/or aluminum values from impure aqueous
phosphoric acid
    • 从不纯的磷酸水溶液中除去镁和/或铝的值
    • US4554144A
    • 1985-11-19
    • US568707
    • 1984-01-06
    • Fernando Ore'
    • Fernando Ore'
    • C01B25/238C01B25/16
    • C01B25/238
    • Magnesium and aluminum impurities are removed from aqueous phosphoric acid by treatment with a fluorine material and an alkali metal containing material in such a manner that the atomic ratio of fluorine to aluminum is adjusted so that it is greater than about 2 and the alkali metal plus magnesium to aluminum atomic ratio to a value no greater than about 2. In one embodiment the fluorine to aluminum ratio is below about 11, preferably between about 4 and about 8. By controlling such atomic ratios in the limits prescribed, a more purified aqueous phosphoric acid can be produced having a substantial reduction in the magnesium and aluminum content thereof. The process is useful for wet-process phosphoric acids. The process is also particularly useful for acids having low P.sub.2 O.sub.5 content and/or high aluminum concentration. The purification process does not require evaporation for the removal of impurities, as for example fluorine as silicon tetrafluoride.
    • 通过用含氟材料和含碱金属的材料处理氟磷与铝的原子比使其大于约2,碱金属加镁,从磷酸水溶液中除去镁和铝杂质 铝原子比为不大于约2.在一个实施方案中,氟与铝的比率低于约11,优选约4至约8.通过将所述原子比控制在规定的限度内,将更纯化的磷酸水溶液 可以制造其镁含量和铝含量显着降低。 该方法可用于湿法磷酸。 该方法对于具有低的P2O5含量和/或高的铝浓度的酸也是特别有用的。 净化过程不需要蒸发去除杂质,例如氟作为四氟化硅。
    • 7. 发明授权
    • Process for extracting tungsten or molybdenum from solution
    • 从溶液中提取钨或钼的工艺
    • US4515756A
    • 1985-05-07
    • US214810
    • 1980-12-09
    • David J. Blumer
    • David J. Blumer
    • C01G39/00C01G41/00C01G49/06
    • C01G49/06C01G39/003C01G41/003C22B3/24Y02P10/234Y10S423/14
    • A process for the recovery of molybdenum and/or tungsten from a solution which comprises the steps of passing said solution through a packed column containing an adsorbent; adsorbing tungsten and/or molybdenum on said adsorbent; passing a solution depleted in tungsten and/or molybdenum from said column; passing a stripping solution through said column containing tungsten and/or molybdenum on said adsorbent to remove tungsten and/or molybdenum with said stripping solution; repeating the first four steps until the stripping solution contains at least about 1 gram per liter of tungsten and/or molybdenum; passing said solution containing at least about 1 gram of tungsten and/or molybdenum per liter into a recovery zone; adjusting the pH of said stripping solution containing at least about 1 gram per liter of tungsten and/or molybdenum to approximately 13.0 by addition of a strong acid and thereby raising the temperature of said solution at least about 10.degree. C.; adding a calcium ion-containing solution to said pH adjusted solution to precipitate calcium tungstate and/or calcium molybdate; and, recovering said tungsten and/or molybdenum as calcium tungstate and/or calcium molybdate.
    • 一种从溶液中回收钼和/或钨的方法,包括使所述溶液通过含有吸附剂的填充柱的步骤; 在所述吸附剂上吸附钨和/或钼; 通过从所述柱中消耗钨和/或钼的溶液; 将剥离溶液通过所述吸附剂上含有钨和/或钼的所述柱,以用所述剥离溶液除去钨和/或钼; 重复前四个步骤,直到汽提溶液含有至少约1克/升的钨和/或钼; 将含有至少约1克钨和/或钼/升的溶液通入所述回收区; 通过加入强酸将每升钨和/或钼至少约1克的所述汽提溶液的pH调节至约13.0,从而将所述溶液的温度升高至少约10℃。 向所述pH调节的溶液中加入含钙离子的溶液以沉淀钨酸钙和/或钼酸钙; 并且将钨和/或钼作为钨酸钙和/或钼酸钙回收。
    • 8. 发明授权
    • Process for making titanium metal from titanium ore
    • 从钛矿制造钛金属的工艺
    • US4468248A
    • 1984-08-28
    • US327320
    • 1981-12-04
    • Joseph A. Megy
    • Joseph A. Megy
    • B22F9/02C22B34/12C22B5/04
    • C22B34/1222B22F9/02C22B34/1277Y02P10/23
    • In a process for the reduction of titanium salt comprising a halide of titanium to titanium metal by contacting said titanium salt in the molten state with a molten alloy and zinc to form a solution of titanium metal in zinc the improvement which comprises the step of:(a) contacting said titanium salt in the molten state with said molten alloy at an elevated pressure to thereby increase the solubility of said titanium metal in said solution.For example, an ore comprising titanium oxides may be fluorinated to convert the titanium oxides to titanium fluorides and the titanium fluorides may be reduced to titanium metal by contacting a molten titanium fluoride salt with a molten zinc-aluminum alloy at an elevated pressure to provide a titanium-zinc alloy having a greater concentration of titanium than is obtained at ambient pressure. The titanium-zinc alloy may be separated from the resulting fluorides of aluminum and the zinc distilled from the alloy to leave behind titanium sponge. The ore may be an ilmenite ore and the fluorination may be carried out by contacting said ilmenite ore with a fluosilicate salt such as sodium fluosilicate.
    • 在通过使熔融状态的所述钛盐与熔融合金和锌接触以形成钛金属在锌中的溶液来将包含钛的卤化物的钛盐还原为钛金属的方法包括以下步骤:( a)在熔融状态下将所述钛盐与所述熔融合金在升高的压力下接触,从而增加所述钛金属在所述溶液中的溶解度。 例如,包含氧化钛的矿石可以被氟化以将钛氧化物转化为氟化钛,并且通过使熔融的氟化钛盐与熔融的锌 - 铝合金在升高的压力下接触将钛氟化物还原成钛金属,以提供 具有比在环境压力下获得的钛浓度更高的钛 - 锌合金。 可以从所得到的铝的氟化物和从合金中蒸馏的锌分离钛 - 锌合金以留下钛海绵。 矿石可以是钛铁矿矿石,并且氟化可以通过使所述钛铁矿矿石与氟硅酸盐如氟硅酸盐接触来进行。
    • 9. 发明授权
    • Method for inhibiting sloughing of unfragmented formation in an in situ
oil shale retort
    • 在原位油页岩蒸馏器中抑制未碎片形成的脱水方法
    • US4444256A
    • 1984-04-24
    • US404475
    • 1982-08-02
    • Jian C. Shen
    • Jian C. Shen
    • E21B43/247E21C41/10
    • E21B43/247E21C41/24
    • A method for igniting an in situ oil shale retort containing a fragmented permeable mass of formation particles containing oil shale is provided. A void space is in the retort between the top surface of the fragmented mass and the top boundary of overlying unfragmented formation. A hot ignition gas comprising oxygen is introduced into the void space to form a combustion zone across the surface of the fragmented mass. An oxygen-supplying gas is then introduced into the void space for sustaining the combustion zone and for advancing the combustion zone downwardly through the retort. The combustion zone is then extinguished and a cool inert gas is introduced into the retort to cool carbonaceous materials comprising the surface of the fragmented mass to a temperature below the self-ignition temperature of such carbonaceous materials, while leaving carbonaceous materials below the fragmented mass surface at temperatures greater than the self-ignition temperature of such materials. Introduction of the inert gas is then discontinued. Thereafter, an oxygen-supplying gas is re-introduced into the retort to ignite the carbonaceous materials below the surface of the fragmented mass for re-establishing the combustion zone in the fragmented mass and for advancing the combustion zone downwardly through the retort.
    • 提供了一种用于点燃原位油页岩蒸馏器的方法,其中包含含有油页岩的地层颗粒的碎片渗透物质。 破碎物质的顶部表面与上覆未破碎地层的顶部边界之间的蒸馏物中的空隙空间。 包含氧气的热点燃气体被引入到空隙空间中,以形成穿过破碎物质的表面的燃烧区域。 然后将供氧气体引入空间空间中,以维持燃烧区域并将燃烧区域向下推进通过蒸馏器。 燃烧区然后熄灭,并且将冷惰性气体引入蒸馏器以将包含碎片物质的表面的含碳材料冷却到低于这种碳质材料的自燃温度的温度,同时将碳质材料留在碎裂的质量表面下方 在大于这种材料的自燃温度的温度下。 然后停止引入惰性气体。 此后,将供氧气体重新引入蒸馏器中以点燃碎片物质表面下方的碳质材料,以重新建立分散物料中的燃烧区域,并将燃烧区域向下推进通过蒸馏器。
    • 10. 发明授权
    • Process for producing phosphorus pentoxide
    • 五氧化二磷生产工艺
    • US4420466A
    • 1983-12-13
    • US376341
    • 1982-05-10
    • Won C. ParkJacob J. Mu
    • Won C. ParkJacob J. Mu
    • C01B25/12C01B25/01C01B25/02C01B25/16
    • C01B25/12
    • A process for producing phosphorus pentoxide from phosphate ore includes the mixing and formulation of a feed mixture of phosphate ore with lime and solid carbonaceous material in amounts to produce a feed mixture having a CaO/SiO.sub.2 mole ratio greater than about 8.0. This mixture is formed into pellets which are then exposed to radiation eminating from an oxidation zone, preferably within a rotary type kiln, in order to heat the pellets to a temperature sufficient to reduce the phosphate by reaction with the solid carbonaceous material to form elemental phosphorus vapor without substantial melting of the pellets. Sufficient oxygen-containing gas is provided to cause oxidation of the elemental phosphorus vapor within the oxidation zone to produce phosphorus pentoxide.
    • 从磷酸盐矿石生产五氧化二磷的方法包括将磷酸盐矿石与石灰和固体碳质材料的进料混合物混合和配制,以产生CaO / SiO 2摩尔比大于约8.0的进料混合物。 该混合物形成颗粒,然后将其暴露于优选在旋转式窑内的氧化区排出的辐射,以便将颗粒加热到足以通过与固体碳质材料反应而还原磷酸盐形成元素磷 蒸汽没有大量熔化的颗粒。 提供足够的含氧气体以引起氧化区内的元素磷蒸气氧化产生五氧化二磷。