公开(公告)号：US20020100718A1

公开(公告)日：2002-08-01

申请号：US10087763

申请日：2002-03-05

申请人： Sharp Kabushiki Kaisha

发明人： Kazuyuki Yamasaki ,  Noriyuki Tanaka ,  Shigeki Matsumoto

IPC分类号： B01D021/30

CPC分类号： C02F3/1215 ,  C02F1/001 ,  C02F1/283 ,  C02F1/5245 ,  C02F1/56 ,  C02F3/302 ,  C02F11/12 ,  C02F2101/14 ,  C02F2101/16 ,  C02F2101/30 ,  C02F2101/301 ,  C02F2209/06 ,  G01N33/18 ,  Y02W10/15 ,  Y10S210/915

摘要： A waste water treatment equipment treats a fluorine waste water containing organic matter, nitrogen, phosphor and hydrogen peroxide by an anaerobic tank 3 in which a calcium carbonate mineral 9 is placed and an aerobic tank 15 in which the calcium carbonate mineral 9 is placed and into which a biologically treated water is introduced from a treatment equipment 444 of another system. Therefore, the fluorine in the waste water can be treated by the calcium carbonate mineral 9 placed in the anaerobic tank 3 and the aerobic tank 15 with the formation of calcium fluoride 11. The organic matter of the surface active agent and so on in the waste water can be treated by the microorganism included in the biologically treated water. Furthermore, nitrate nitrogen can be treated so as to be reduced to a nitrogen gas in the anaerobic tank 3, while ammoniacal nitrogen and nitrite nitrogen can be treated so as to be oxidized in the aerobic tank 15. That is, the waste water treatment equipment can highly efficiently treat the surface active agent, nitrogen, polychlorinated aluminum, macromolecular coagulant, hydrogen peroxide and phosphor in the waste water, by which the waste can be reduced.

公开(公告)号：US20040188348A1

公开(公告)日：2004-09-30

申请号：US10824505

申请日：2004-04-15

申请人： Sharp Kabushiki Kaisha

发明人： Kazuyuki Yamasaki ,  Kazumi Chujo ,  Hiroyuki Ishibashi

IPC分类号： C02F009/00

CPC分类号： C02F9/00 ,  B01D61/025 ,  B01D61/142 ,  B01D61/145 ,  B01D61/16 ,  B01D61/18 ,  B01D61/58 ,  B01D63/16 ,  B01D65/08 ,  B01D2311/04 ,  B01D2311/16 ,  B01D2315/06 ,  B01D2321/04 ,  B01D2321/185 ,  B01D2321/2058 ,  C02F1/04 ,  C02F1/283 ,  C02F1/32 ,  C02F1/441 ,  C02F1/444 ,  C02F1/469 ,  C02F1/5236 ,  C02F1/66 ,  C02F1/722 ,  C02F1/74 ,  C02F3/34 ,  C02F2101/103 ,  C02F2103/12 ,  C02F2209/06 ,  B01D2311/12 ,  B01D2311/18 ,  B01D2311/2642

摘要： This metal containing waste water treatment method introduces a metal containing waste water from above into a submerged membrane separation tank 1 in which a reaction section 2, a submerged membrane section 3 having a submerged membrane 5 and a precipitation section 4 are arranged in order from top to bottom, causes a reaction by adding a pH adjuster to the reaction section 2, subsequently separates water from metal by the submerged membrane 5 of the submerged membrane section 3 and subsequently precipitates and concentrates the metal in the precipitation section 4. As described above, according to this treatment method, the pH adjuster is added to the reaction section 2, and therefore, solid-liquid separation can be effected by the submerged membrane 5 with a hydroxide formed. Moreover, the metal can be precipitated and concentrated by the action of gravity without using energy in the precipitation section 4.

摘要翻译： 该含金属废水处理方法将含有金属的废水从上面引入浸没式膜分离槽1中，其中反应部分2，具有浸没膜5和沉淀部分4的浸没膜部分3从顶部顺序排列 通过向反应部2添加pH调节剂而引起反应，接着通过浸没膜部3的浸没膜5将金属分离并随后沉淀并浓缩析出部4中的金属。如上所述， 根据该处理方法，向反应部2添加pH调节剂，因此可以通过形成有氢氧化物的浸没膜5进行固液分离。 此外，金属可以通过重力的作用而沉淀和浓缩，而不会在沉淀部分4中使用能量。

公开(公告)号：US20020144940A1

公开(公告)日：2002-10-10

申请号：US10160183

申请日：2002-06-04

申请人： Sharp Kabushiki Kaisha

发明人： Kazuyuki Yamasaki ,  Kazumi Chujo ,  Seiji Okamoto ,  Yukihiro Tao

IPC分类号： B01D033/70

CPC分类号： C02F3/30 ,  C02F1/001 ,  C02F1/441 ,  C02F1/444 ,  C02F1/5245 ,  C02F1/5281 ,  C02F1/56 ,  C02F2101/10 ,  C02F2101/105 ,  C02F2101/14 ,  C02F2101/16 ,  C02F2101/30 ,  C02F2103/346 ,  Y10S210/908 ,  Y10S210/911 ,  Y10S210/915 ,  Y10S210/919

摘要： An apparatus for treatment of fluorine waste water has an introduction tank, a main treatment tank, a calcium hydroxide tank, a polychlorinated aluminum tank, a macromolecular flocculant tank, a settling tank, and a concentration tank. Fluorine waste water is introduced through the introduction tank into a lower part of the main treatment tank. Also, return sludge from the concentration tank and silicon sludge from a silicon waste water treatment system are introduced into an upper part of the main treatment tank. Thus, silicon recovered from silicon waste water is recycled for treatment of fluorine waste water. Also, unreacted chemicals, which have been loaded in the calcium hydroxide tank, polychlorinated aluminum tank, macromolecular flocculant tank, are recycled. The main treatment tank has no stirrer, but can neutralize the waster water.

摘要翻译： 用于处理氟废水的设备具有导入槽，主处理槽，氢氧化钙罐，多氯化铝罐，大分子絮凝罐，沉淀槽和浓缩罐。 氟废水通过导入罐引入主处理槽的下部。 此外，将来自浓缩罐的污泥和来自硅废水处理系统的硅污泥引入主处理槽的上部。 因此，从硅废水回收的硅被再循环用于处理氟废水。 此外，已经装载在氢氧化钙罐，多氯化铝罐，大分子絮凝剂罐中的未反应的化学品被再循环。 主处理槽没有搅拌器，但可以中和废水。