Selective removal of contaminants from water sources using inorganic
media
    1.
    发明授权
    Selective removal of contaminants from water sources using inorganic media 失效
    使用无机介质从水源中选择性去除污染物

    公开(公告)号:US5078889A

    公开(公告)日:1992-01-07

    申请号:US598987

    申请日:1990-10-17

    Abstract: A process using a regenerable inorganic media capable of removing contaminants by catalytic oxidation or reduction, as well as heavy metal adsorption, from well and surface water sources. The specific material is specially-treated gamma-type electrolytic manganese dioxide, the treatment involving comminuting to a 20-60 mesh size, complete neutralization and washing to remove fines, residual acidity and neutralization products. Certain taste, odor and staining water contaminants such as hydrogen sulfide, iron and manganese can be oxidized and filtered by the media with subsequent removal from the system by simply backwashing with water or water in combination with simple chemicals. Heavy metals are removed by a different adsorption mechanism on the same media followed by regeneration with a dilute acid. Pretreatment of the media with sodium hydrosulfite further allows the removal of residual chlorine. This product demonstrates a high degree of selectivity and a high capacity for all three types of contaminants. The results of the treatment of water solutions containing a wide variety of contaminants are given showing that most of the contaminants are readily removed to levels established by the U.S. Environmental Protection Agency for drinking water. The inorganic catalytic oxidizing/reducing and adsorbent material can be placed in larger canisters for point of entry use or in smaller cartridges for point of use applications, depending upon the particular requirement.

    Abstract translation: 使用可再生无机介质的方法,该无机介质能够从井和地表水源通过催化氧化或还原以及重金属吸附除去污染物。 具体材料是经特殊处理的γ型电解二氧化锰,粉碎处理至20-60目尺寸,完全中和洗涤,除去细粉,残留酸度和中和产物。 某些味道,气味和染色的水污染物如硫化氢,铁和锰可以被介质氧化和过滤,随后通过简单地用水或水与简单的化学物质反洗,从体系中除去。 重金属通过不同的吸附机理在相同介质上除去,然后用稀酸再生。 用连二亚硫酸钠预处理介质进一步允许去除残留的氯。 该产品对所有三种类型的污染物表现出高度的选择性和高容量。 给出了处理含有各种污染物的水溶液的结果,显示大多数污染物容易被除去到美国环境保护局为饮用水建立的水平。 根据具体要求,无机催化氧化/还原和吸附剂材料可以放置在用于入口使用的较大的罐中或用于使用点的较小的筒中。

    Preferential removal of ammonia and phosphates
    2.
    发明授权
    Preferential removal of ammonia and phosphates 失效
    优先除氨和磷酸盐

    公开(公告)号:US3984313A

    公开(公告)日:1976-10-05

    申请号:US570141

    申请日:1975-04-21

    Inventor: Irwin R. Higgins

    Abstract: Sewage water containing many pollutants including ammonia and phosphates is treated so that the ammonia and phosphates are preferentially removed through ion exchange while the other contaminants are allowed to remain in the water. Ferric hydroxide is deposited within the matrix of strong acid type cation exchange resin and the resin is rejuvenated with sodium hydroxide.

    Abstract translation: 处理含有氨和磷酸盐的许多污染物的污水,以便通过离子交换优先除去氨和磷酸盐,而允许其他污染物留在水中。 氢氧化铁沉积在强酸型阳离子交换树脂的基体内,树脂用氢氧化钠还原。

    Simultaneous electro-deposition of manganese and manganese dioxide
    3.
    发明授权
    Simultaneous electro-deposition of manganese and manganese dioxide 失效
    同时电沉积锰和二氧化锰

    公开(公告)号:US4707227A

    公开(公告)日:1987-11-17

    申请号:US907509

    申请日:1986-09-15

    Inventor: Irwin R. Higgins

    CPC classification number: C25B1/21 C25C1/10

    Abstract: An electro-deposition process for simultaneously producing manganese metal and manganese dioxide. Manganese metal and manganese dioxide are simultaneously electro-deposited in an electrolytic cell without the use of membranes separating the anode and cathode compartments. This is accomplished using a manganese chloride electrolyte in a temperature range of about 70 to 90 degrees C., with the free hydrochloride acid being removed from the electrolyte to a level below about 0.1M. The acid removal can be accomplished, for example, with an acid retardation step involving the use of strong base ion exchange resins in the preferred form. This is carried out in a continuous countercurrent current ion exchanger such that the molarity of the electrolyte is achieved with the acid being removed. The process described is suitable for the economical electro-deposition of manganese metal and manganese dioxide from leach solutions obtained from relatively low assay ores having of the order of 10 percent manganese. The current density and current efficiency are such that an economical process is achieved that is competitive with the processes of the prior art utilizing high grade ores.

    Abstract translation: 一种同时生产锰金属和二氧化锰的电沉积工艺。 锰金属和二氧化锰同时电解沉积在电解槽中,而不使用隔离阳极和阴极隔室的膜。 这是使用在约70至90℃的温度范围内的氯化锰电解质完成的,游离的盐酸从电解质中除去至低于约0.1M的水平。 酸除去可以例如通过使用强碱性离子交换树脂优选形式的酸性延迟步骤来实现。 这在连续逆流电流离子交换器中进行,使得电解质的摩尔浓度通过除去酸来实现。 所述方法适用于从具有约10%锰的较低测定矿石获得的浸出溶液中经济地电沉积锰金属和二氧化锰。 当前的密度和电流效率使得获得与现有技术利用高等级矿石的方法竞争的经济的方法。

    Extraction of thermally stable contaminants from stack gas scrubbing
amines
    4.
    发明授权
    Extraction of thermally stable contaminants from stack gas scrubbing amines 失效
    从烟气洗涤胺中提取热稳定的污染物

    公开(公告)号:US5277822A

    公开(公告)日:1994-01-11

    申请号:US887041

    申请日:1992-05-22

    Inventor: Irwin R. Higgins

    CPC classification number: B01J47/10 B01D53/1425

    Abstract: A process for the removal of thermally-stable contaminants from stack gas scrubbing amines using a continuous countercurrent ion exchange column. Amines contaminated after use in stack gas scrubbing are fed into the column containing an anion exchanger resin where the contaminants are sorbed on the resin. The amine is washed from the resin with hot water and is removed from the column. The resin is then pulsed to move the resin with the sorbed contaminants into a elution section of the column. The contaminants are removed using an eluant of sodium hydroxide solution, preferably containing chlorine to enhance elution of thiocyanate ion. A water wash removes traces of the hydroxide solution and any reaction products, and then the resin is again pulsed so as to be moved for reuse. The amines are regenerated with only the single type resin (preferably Type I) and with significantly reduced quantity of reagents.

    Abstract translation: 使用连续的逆流离子交换柱从堆叠气体洗涤胺中除去热稳定的污染物的方法。 在烟道气洗涤中使用后被污染的胺进料到含有污染物被吸附在树脂上的阴离子交换树脂的柱中。 用热水从树脂中洗涤胺并从柱中除去。 然后将树脂脉冲以将具有吸附的污染物的树脂移动到塔的洗脱部分。 使用氢氧化钠溶液的洗脱剂除去污染物,优选含氯,以增强硫氰酸根离子的洗脱。 水洗除去痕量的氢氧化物溶液和任何反应产物,然后再次将树脂脉冲以便移动以重新使用。 胺仅用单一类型的树脂(优选I型)再生,并且试剂量显着减少。

    Regenerable inorganic media for the selective removal of contaminants
from water sources
    5.
    发明授权
    Regenerable inorganic media for the selective removal of contaminants from water sources 失效
    用于从水源中选择性去除污染物的可再生无机介质

    公开(公告)号:US5082570A

    公开(公告)日:1992-01-21

    申请号:US633029

    申请日:1990-12-24

    Abstract: A regenerable inorganic media capable of removing contaminants by catalytic oxidation or reduction, as well as heavy metal adsorption, from well and surface water sources. The specific material is specially-treated microporous battery grade gamma-form electrolytic manganese dioxide, the treatment involving comminuting to a 20-60 mesh size, complete neutralization and washing to remove fines, residual acidity and neutralization products. Certain taste, odor and staining water contaminants such as hydrogen sulfide, iron and manganese can be oxidized and filtered by the media with subsequent removal from the system by simply backwashing with water or water in combination with simple chemicals. Heavy metals are removed by a different adsorption mechanism on the same media followed by regeneration with a dilute acid. Pretreatment of the media with sodium hydrosulfite further allows the removal of residual chlorine. This product demonstrates as high degree of selectivity and a high capacity for all three types of contaminants. The inorganic catalytic oxidizing/reducing and adsorbent material can be placed in larger canisters for point of entry use or in smaller cartridges for point of use applications, depending upon the particular requirement.

    Abstract translation: 一种可再生的无机介质,能够通过催化氧化或还原以及来自井和地表水源的重金属吸附来除去污染物。 具体材料是特殊处理的微孔电池级γ型电解二氧化锰,处理方式为粉碎至20-60目尺寸,完全中和洗涤,除去细粉,残留酸度和中和产物。 某些味道,气味和染色的水污染物如硫化氢,铁和锰可以被介质氧化和过滤,随后通过简单地用水或水与简单的化学物质反洗,从体系中除去。 重金属通过不同的吸附机理在相同介质上除去,然后用稀酸再生。 用连二亚硫酸钠预处理介质进一步允许去除残留的氯。 该产品为所有三种类型的污染物表现出高度的选择性和高容量。 根据具体要求,无机催化氧化/还原和吸附剂材料可以放置在用于入口使用的较大的罐中或用于使用点的较小的筒中。

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