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    • 3. 发明专利
    • DISPOSAL OF WASTE WATER
    • JPS5712893A
    • 1982-01-22
    • JP8680880
    • 1980-06-26
    • MITSUBISHI HEAVY IND LTD
    • YAMAUCHI TOORUUEDA RIYOUHEIKAYANO ISAMUTSUSHIMA TAKETOSHIFUKUNAGA KAZUO
    • C02F3/34
    • PURPOSE:To obtain dischargeable purified water with high efficiency, by adding an NO2 salt to waste water containing NH4 , polythionic acid, S-N compounds, etc., oxidizing the waste water with sludge containing sulfur bacteria and nitrifying bacteria, and then reducing nitrogen compounds in the waste water to N2 gas. CONSTITUTION:Waste water containing NH4 , NO2 , NO3 , polythionic acid and S-N compounds is introduced into a disposal vessel 3.The waste water in the vessel 3 is kept at pH about 4 or less and a temperature of about 60 deg.C or higher. NO2-N, having a concentration at least equal to an expected N concentration of the S-N compounds, is fed to the waste water, and the waste water is agitated to decompose the S-N compounds into N2 or N2O gas and SO4 . The treated waste water is let flow into a pH-adjusting vessel 4, where the waste water is neutralized at pH about 6-8. Thereafter, the waste water is oxidized by sulfur bacteria in an aerobic disposal vessel 11 containing a sulfur compound, e.g. SCN- or the like, as a nutritious source. the waste water is further introduced into an anaerobic denitrifying vessel 2 containing denitrifying bacteria, where the waste water is agitated and fluidized to reduce most of NO2 to N2 gas.
    • 4. 发明专利
    • Anaerobic digestion method
    • ANAEROBIC DIGESTION方法
    • JPS58205594A
    • 1983-11-30
    • JP8724382
    • 1982-05-25
    • Mitsubishi Heavy Ind Ltd
    • UEDA RIYOUHEIFUKUNAGA KAZUO
    • C02F11/04
    • Y02E50/343
    • PURPOSE: To improve the recovery rate of gaseous methane, dehydration efficiency, etc., by subjecting the excess sludge produced by an aerobic biological treatment to the heat treatment at 80W200°C then to solid-liquid sepn. and subjecting the separated liquid thereof to an anaerobic digestion treatment.
      CONSTITUTION: Raw sludge 5 is supplied through a concentrator (d') and a concd. raw sludge line 20 into the 1st digestion tank (e). On the other hand, excess sludge 6 is concentrated separately from the sludge 5 in the concentrator (d") and is then fed through a concd. excess sludge line 21 into a heat treatment device (h), where the sludge is heat-treated to 80W200°C and the treated sludge is introduced through a line 22 into a thickener (i). The sludge is divided to supernatant liquid 24 and settled sludge 23; the sludge 23 is further divided with a dehydration installation (g') to dehydrated cake 25 and separated liquid 26. The liquid 24 and the liquid 26 are supplied to the 1st anaerobic digestion tank (e).
      COPYRIGHT: (C)1983,JPO&Japio
    • 目的:为了提高气体甲烷的回收率,脱水效率等,将需氧生物处理产生的多余污泥进行80-200℃的热处理,然后进行固液分离。 并对其分离的液体进行厌氧消化处理。 构成:原料污泥5通过浓缩器(d')和浓缩器 原料污泥管线20进入第一消化槽(e)。 另一方面,多余的污泥6与浓缩器(d“)中的污泥5分开浓缩,然后通过浓缩物(d”)进料。 多余污泥管线21进入热处理装置(h),其中将污泥热处理至80-200℃,并将经处理的污泥通过管线22引入增稠剂(i)。 将污泥分为上清液24和沉淀污泥23; 将污泥23进一步与脱水装置(g')分离成脱水饼25和分离的液体26.液体24和液体26被供给到第一厌氧消化罐(e)。
    • 5. 发明专利
    • Method for treating waste water by microorganism
    • 微生物处理废水的方法
    • JPS5771695A
    • 1982-05-04
    • JP14711280
    • 1980-10-21
    • Mitsubishi Heavy Ind Ltd
    • YAMAUCHI TOORUUEDA RIYOUHEISATOU ARATAASAGI MASAAKIFUKUNAGA KAZUO
    • C02F3/00
    • PURPOSE: To enable to perform a stable waste water treatment utilizing special microorganism by a method wherein microorganism is frozen in a low-temperature region, it is then dried by keeping it in room-temperature conditions, is stored in a condition of being shielded from the outside air, and thereafter it is used as required.
      CONSTITUTION: Waste water 12 is introduced into a treating tank 2, in which it is contacted to microorganism, then the waste water is fed into a precipitating tank 3, in which the microorganism is separated by precipitation an is drawn out at a bottom part of the tank 3. The supermatent water 13 in the tank 3 is discharged or after-treated. The microorganism 14 drawn out from the tank 3 is returned as return microorganism 14a into the tank 2 via a return line 4, while excesses 14b, 14c of microorganism are directed into a microorganism tank 6 and is temporarily stored therein. Then, the microorganism 15 concentrated by a concentrating means 7 is frozen in a low temperature region of -20°C or below by a freezing means 8. The frozen microorganism 16 is heated to the room-temperature condition in a closed container while evacuating container by a vacuum pump so as to dry the microorganism to a water content of 10% or below. The thus dried microorganism 17 is transferred into a staring container and is left to stand still at a storing plate 10. The dried microorganism 18 thus stored is charged into the tank 2, as required.
      COPYRIGHT: (C)1982,JPO&Japio
    • 目的:为了能够通过微生物在低温区域中冷冻的方法,利用特殊微生物进行稳定的废水处理,然后通过将其保持在室温条件下进行干燥,在被屏蔽的条件下储存 外部空气,然后根据需要使用。 构成:将废水12引入到与微生物接触的处理槽2中,然后将废水送入沉淀池3中,其中微生物通过沉淀分离,在底部被抽出 罐3中的超级水13被排出或后处理。 从罐3排出的微生物14作为回收微生物14a通过返回管线4返回到罐2中,微生物的过量14b,14c被引导到微生物罐6中并暂时存储在其中。 然后,通过浓缩装置7浓缩的微生物15通过冷冻装置8在-20℃以下的低温区域中冷冻。将冷冻微生物16在密闭容器中加热至室温条件,同时抽真空 通过真空泵将微生物干燥至含水量为10%以下。 将如此干燥的微生物17转移到凝露的容器中并静置在储存板10上。如此存储的干燥微生物18根据需要装入罐2中。