会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 发明专利
    • TREATMENT OF WASTE WATER
    • JPH06114391A
    • 1994-04-26
    • JP29084592
    • 1992-10-05
    • NIPPON KOKAN KK
    • YAMAMOTO MASAAKIMIYAKE MINORUMAKI AKIRAYAMATE YOSHITOMOKOYAMA KAZUHIDEMAEDA KOZO
    • C02F3/12G01N33/18
    • PURPOSE:To stabilize activated sludge in waste water by quantitatively measuring the states of filamentous bacteria and agglutinative bacteria contained in activated sludge in waste water by an image processor and controlling the characteristics of both bacteria on the basis of the measured result. CONSTITUTION:The image of activated sludge is automatically measured at every 10min to 1hr by the submerged microscope 4b arranged in an aeration tank 1 and image processing and operation are executed by an image processor 5 and an operation device 6. By the image processing, the predetermined items related to filamentous bacteria and agglutinative bacteria in the bacteria constituting activated sludge, that is, the length of filamentous bacteria and the area, brightness, area distribution and brightness distribution of agglutinative bacteria are measured and the measured data are introduced into the operation device 6 and operation judgment is performed on the basis of the knowledge base of the device 6. From the judge results, the characteristics of filamentous and agglutinative bacteria are controlled by the alteration of the setting of an inflow water flow rate and an aeration air amt. and the activated sludge in waste water can be stabilized.
    • 3. 发明专利
    • PRODUCTION OF GRANULAR AMMONIUM SULFATE
    • JPH0881215A
    • 1996-03-26
    • JP21682794
    • 1994-09-12
    • NIPPON KOKAN KK
    • MIYAKE MINORU
    • C01C1/24
    • PURPOSE: To make continuous liquid circulation between two steps of absorption and crystallization unnecessary by suppressing free sulfuric acid concentration in the mother liquor of ammonium sulfate in a method for producing ammonium sulfate from ammonium in gas of a coke oven. CONSTITUTION: Two spray type saturating towers 2 and 3 are provided in series in an adsorption step. A part of a coke oven gas reacted in the first saturating tower 2 is again reacted with a part of mother liquor of ammonium sulfate in the second saturating tower 3. When the concentration of free sulfuric acid in the mother liquor in a crystallization step becomes a prescribed concentration, production of granular ammonium sulfate in the crystallizing step is temporally stopped and whole crystals attached to the crystallizing apparatus are dissolved and the mother liquor of ammonium sulfate in the crystallization step is transferred to the first saturating tower 2 and exchanged for mother liquor of ammonium sulfate having low free sulfuric acid concentration and charged from the second saturating tower 3, and then, production of granular ammonium sulfate in the crystallization step is reopened. Consequently, continuous circulation of the mother liquor between two steps of the adsorption and crystallization is made unnecessary. Operational days can be extended to be 2-3 times longer than that o.f conventional method.
    • 5. 发明专利
    • PRODUCTION OF GYPSUM FROM COKE OVEN GAS
    • JPH03247510A
    • 1991-11-05
    • JP4369490
    • 1990-02-23
    • NIPPON KOKAN KK
    • MIZUSAWA MASATOSHISUMIKAMA TAKASHIMIYAKE MINORU
    • C01F11/46
    • PURPOSE:To produce gypsum large in mean crystalline particle diameter by specifying both pH value of hydrogen calcium sulfite slurry introduced into an oxidation tower and pH value of gypsum slurry discharged from the oxidation tower. CONSTITUTION:Coke oven gas is desulfurized and sulfur contained in the obtained waste liquid is burned. The combustion exhaust gas contg. SO2 is introduced into an absorption tower 1 and SO2 is absorbed into the prescribed amount of Ca(OH)2 soln. to produce hydrogen calcium sulfite slurry. This slurry is introduced into an oxidation tower 3 via a tank 2 and air is blown thereinto from the lower part. The slurry is oxidized to obtain gypsum slurry and gypsum 6 is obtained via a thickner 4 and a separator 5. At this time, Ca(OH)2 slurry is added to hydrogen calcium sulfite slurry in the tank 2 and pH value is regulated to 3.2-3.7. H2SO4 is added to gypsum slurry in the thickner 4 and pH value is regulated to 2.0-2.2. Thereby gypsum 6 is obtained which has about 30-40mum mean crystalline particle diameter and is excellent in quality and high in commodity value.