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    • 1. 发明专利
    • TREATMENT OF ARSENIC-CONTAINING SLUDGE
    • JPH10128396A
    • 1998-05-19
    • JP28662396
    • 1996-10-29
    • MITSUBISHI HEAVY IND LTD
    • FUJITA HIROSHITAO KOZOSHIMIZU HIROSHIYOKOSE MAMORU
    • C02F1/62C02F1/52C02F1/66C02F11/00C02F11/12C02F11/14
    • PROBLEM TO BE SOLVED: To surely prevent the re-elution of arsenic at a time when arsenic-containing sludge is subjected to disposal treatment by adding a calcium compd. to arsenic- containing waste water to adjust the waste water to a specific pH value and subjecting this waste water to solid-liquid separation treatment to obtain arsenic-containing sludge and adding slaked lime to the sludge before calcinating the sludge. SOLUTION: When slaked lime 12 is added to arsenic-containing waste water 11 flowing in a first reaction tank 1 to adjust the pH of the waste water to 12 or more, hydroxide flocs are formed. Next, this reaction soln. is subjected to solid-liquid separation within a flocculation and sedimentation tank 2 to form flocculated sedimented sludge 17 and a part of this sludge 17 is returned to the first reaction tank 1 as return sludge 17a and the remainder is stored in a sludge storage tank 5. When the sludge in the storage tank 5 becomes a definite amt., the sludge is dehydrated by a dehydrator 6 to be dried by a dryer 7 and, after slaked lime 9 is added to the dried sludge, the lime added sludge is calcined in a calcinator 8. The treated soln. of the sedimentation tank 2 is introduced into a second reaction tank 3 and an iron salt and an acid are added to the treated soln. to convert residual arsenic to iron arsenate which is, in turn, included in ferric hydroxide flocs formed at the same time to be co-precipitated.
    • 6. 发明专利
    • FLUE GAS TREATMENT SYSTEM
    • JPH09173767A
    • 1997-07-08
    • JP33855995
    • 1995-12-26
    • SUYAMA TAKAZOMITSUBISHI HEAVY IND LTD
    • SUYAMA TAKAZOSUZUMURA HIROSHIOGUSHI YASUYUKIUGAWA NAOHIKOHINO MASAOTAO KOZOKOJIMA NOBUOOKAZOE KIYOSHI
    • B01D53/34B01D53/50B01D53/64B01D53/77
    • PROBLEM TO BE SOLVED: To facilitate the treatment of Se in a flue gas by providing the system with a means for subjecting a flue dust slurry to which an insolubilizer and an adsorbent are added, to solid-liquid separation. SOLUTION: In this system, dust contg. Se stuck thereto is collected and removed from a flue gas by using an electrostatic precipitator 5 or the like and then, subjected to extraction treatment with a liquid supplied from a wet desulfurization equipment 20 in an extraction means 13 to extract soluble components in the dust and to form a dust slurry. Thereafter, an insolubilizer A that is used for insolubilizing at least quadrivalent Se and supplied from an insolubilizer supply means 16, is added to the dust slurry in a mixing means 14 and further, an adsorbent X that is used for adsorbing at least hexavalent Se and supplied from an adsorbent supply means 100 is added to the resulting dust slurry in another mixing means 101 and then, the dust slurry contg. the insolubilizer and adsorbent is subjected to solid-liquid separation with a separation means 15 to separate quadrivalent and hexavalent Se in the solid phase from the liquid phase. At that time, each of a slurry withdrawal line of the desulfurization unit 20 and a wastewater treatment equipment 50 is similarly provided with a mixing device 14, an insolubilizer supply means 16, another mixing means 101, an adsorbent supply means 100 and a separation means. Moreover, in the desulfurization equipment 20, minimum required oxidation is performed by using an oxidation-reduction potential control method to inhibit oxidation of quadrivalent Se to hexavalent Se from occurring and to facilitate the Se treatment in the wastewater treatment equipment 50, etc. As the adsorbent X, an organismic raw material such as eggshell membrane or feather is used and as the insolubilizer A, FeCl3 or Fe(SO4 )3 is used.
    • 8. 发明专利
    • METHOD FOR MEASURING VOLATILE MATERIAL IN HIGH-VISCOSITY MATERIAL
    • JPS61251755A
    • 1986-11-08
    • JP9314485
    • 1985-04-30
    • MITSUBISHI HEAVY IND LTD
    • UEDA TAKASHINAKANE TAKEMITAO KOZO
    • G01N25/14G01N25/00
    • PURPOSE:To make quantitative determination with high accuracy by adding an org. solvent which does not responds to a hydrogen flame ionization detector to a sample to dilute the sample, injecting the sample to an evaporation part set at a prescribed temp. and measuring the evaporated volatile material and org. solvent in a detecting part. CONSTITUTION:The hydrogen flame ionization detector is constituted of a box 1 for evaporation contg. a heater for heating and a detecting part 2. The sample 3 diluted by the org. solvent is injected through an injection port 4 by as much as several mul into a flow passage 5 in the box 1. The sample is heated by the heater and the volatile material and the org. solvent for dilution evaporate. On the other hand, nitrogen 6 which is an inert gas is supplied from a flow passage 7 into a flow passage 5 and the evaporated volatile material and the org. solvent for dilution are introduced to the part 2. Air 8 and hydrogen 9 are supplied to the part 2 to burn the volatile material and the org. solvent for dilution. The C ions originating from the volatile material are detected by a pair of electrodes 10. The quantitative determination of the volatile material with high accuracy is thus made possible.