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
    • Sludge treating method
    • 泥沙处理方法
    • JPS59216700A
    • 1984-12-06
    • JP9174083
    • 1983-05-24
    • Toray Eng Co Ltd
    • AZUMA SHINJISHIMADA KAZUOTAKEDA FUKUTAKAOSADA TAKESHI
    • C02F11/14
    • PURPOSE: To still more lower the water content of a cake and to accelerate the filtering speed thereof, by performing the dehydration of sludge during a time when the pH of the sludge in which a limestone powder is added and mixed is held in an acidic region.
      CONSTITUTION: Raw water 1 is sent to a flocculation tank 2 and subjected to flocculation treatment while aluminum sulfate 3 is added to and mixed in said raw water. Subsequently, this water subjected to flocculation treatment is sent to a precipitation tank 4 to be subjected to solid-liquid separation and sludge 5 is sent to a post-treatment process 8 for performing filtration or the like to be treated so as to obtain predetermined water quality while the treated water is sent to a factory or a home. In this case, the sludge 5 from purified water is sent to an acid treating tank 6 where sulfuric acid 9 is added to and mixed in said sludge 5 to adjust the pH thereof to 1W3 and the acidified sludge is subsequently sent to a precipitative precipitation tank 10 to be subjected to solid- liquid separation while the conc. sludge 14 is sent to a dehydration aid adding tank 12 to be mixed with a limestone powder 13 under stirring and the resulting mixture is converted to a cake in a dehydration process 14.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:为了进一步降低滤饼的含水量并加速其过滤速度,通过在添加和混合石灰石粉末的污泥的pH保持在酸性区域的时间内进行污泥的脱水, 。 构成:将原水1送入絮凝槽2,进行絮凝处理,同时加入硫酸铝3并混合在原水中。 随后将经过絮凝处理的水送入析出槽4进行固液分离,并将污泥5送入后处理工序8进行处理的过滤等,得到规定的水 处理过的水被送到一个工厂或一个家中时,质量很好。 在这种情况下,将来自纯化水的污泥5送入酸处理槽6,在其中加入硫酸9并在所述污泥5中混合,将pH调节至1-3,随后将酸化的污泥送入沉淀 沉淀池10要进行固液分离, 将淤渣14送到脱水助剂添加罐12中,与搅拌下的石灰石粉13混合,将得到的混合物转化成脱水工序14中的滤饼。
    • 2. 发明专利
    • Incineration of waste ion exchange resin
    • 废物离子交换树脂的焚烧
    • JPS5913823A
    • 1984-01-24
    • JP12402982
    • 1982-07-15
    • Toray Eng Co Ltd
    • OSADA TAKESHIYAMADA TADAO
    • F23G7/00F23G5/02F23K5/12G21F9/32
    • F23G5/02
    • PURPOSE:To dispense with the pre-treatment of waste ion exchange resin such as pulverization of the resin, to incinerate the resin efficiently and to reduce the quantity of resultant exhaust gas by a method wherein the wet and coarse waste ion exchange resin is mixed with fuel oil and water in the presence of an emulsifier to produce oil drop-in-water three component type stabilized emulsion and the emulsion is burned by spraying. CONSTITUTION:Wet and coarse waste ion exchange resin 12 is mixed with fuel oil 10 and water 11 in the presence of emulsifier 13 to thereby produce oil drop- in-water three component type stabilized emulsion. The emulsion thus produced is transferred from a tank 1 through a pump 2 and burned by spraying it into a furnace 4 through a nozzle 3. Further, an auxiliary fuel is supplied through a pump 5 and a nozzle 6.
    • 目的:为了省去树脂粉碎等废弃物离子交换树脂的预处理,能够有效地焚化树脂,通过将粗废废离子交换树脂与 燃料油和水在乳化剂存在下生产油包水型三组分型稳定化乳液,并通过喷雾燃烧乳液。 构成:将湿粗废废物离子交换树脂12在乳化剂13的存在下与燃料油10和水11混合,由此生成油包水型三组分型稳定化乳液。 由此产生的乳液从罐1通过泵2转移并通过喷嘴3喷射到炉4中而燃烧。此外,通过泵5和喷嘴6供给辅助燃料。
    • 3. 发明专利
    • PURIFICATION OF HEAVY METAL AMMINE COMPLEX-CONTAINING LIQUID
    • JPS5814992A
    • 1983-01-28
    • JP11110981
    • 1981-07-15
    • TORAY ENG CO LTD
    • BABA YASUOOSADA TAKESHI
    • C02F1/62
    • PURPOSE:To further enhance heavy metal-removing efficiency, by adding orthophosphoric ion-forming substance only or in company with a flocculant to the titled liquid and then adjusting the pH value of the liquid, to remove heavy metals from the liquid. CONSTITUTION:Substance, e.g. orthophosphoric acid or its alkali metal salt, which will form an orthophosphoric ion in a heavy metal ammine complex-contg. liquid, is added to the liquid. A flocculant in company with one or more kinds of the substances may be added to the liquid. In this case, the flocculant may be added as a liquid mixed with the substance. The flocculant is preferably one or more of sulfates, chlorides or the like of Fe, Al and Ca, e.g. FeCl3, Al2(SO4)3 and CaCl2. When the concentration of the heavy metal ammine complex is low, said conjunct use is desirable. After the liquid is mixed with these additives, the liquid is adjusted at a neutral pH level by addition of a mineral acid or alkali. Consequently, the heavy metals are converted into an insoluble state and precipitated. The precipitated heavy metals are separated from the liquid.
    • 7. 发明专利
    • DUST REMOVING METHOD
    • JPS61278324A
    • 1986-12-09
    • JP12003985
    • 1985-06-03
    • TORAY ENG CO LTD
    • OSADA TAKESHIYAMADA TADAOKONISHI KENICHIHAMADA YOSHIHISA
    • B01D47/10
    • PURPOSE:To perform the dust removal of gas contg. great quantities of steam by sending the gas in the order of the first venturi scrubber, a gas cooler and the second venturi scrubber and treating it. CONSTITUTION:A high-temp. radioactive exhaust gas G1 sent from an incinerator is cooled in a underwater bubbling type scrubber 1 and both the cooling of the above-mentioned gas G1 and the primary removal of the contained minute grain are performed herein. Then the radioactive gas G2 contg. the great quantities of steam which are produced in the water washing is sent too the first venturi scrubber 2 to perform the secondary removal. Successively the radioactive exhaust gas G3 having a state saturated with steam discharged therefrom is sent to a gas cooler 4 via the first mist separator 3. Therein the grain size of the steam is increased while keeping the minute grain which is not removed in the scrubber 2 as a nucleus. Therefore the minute grain incorporated in the gas G5 sent to the following second venturi scrubber 5 can be effectively removed.
    • 8. 发明专利
    • METHOD FOR CONCENTRATING AND RECOVERING ORGANIC VALUABLES
    • JPS60132604A
    • 1985-07-15
    • JP24075183
    • 1983-12-19
    • TORAY ENG CO LTD
    • BABA YASUOOSADA TAKESHI
    • B01D61/02B01D61/12B01D61/14B01D61/22
    • PURPOSE:To selectively concentrate valuables from an aqueous solution containing inorg. salts and low MW org. valuables, by subjecting an aqueous solution to be treated to membrane separation treatment, which uses a separation membrane or which the salt exhaustive ratio under operation pressure of osmotic pressure of less of said solution is specific value or more, under operating pressure of osmotic pressure or more. CONSTITUTION:A separation membrane having separation capacity capable of obtaining a salt exhaustive ratio of 5% or less when membrane separation treatment is applied to an aqueous solution to be treated under operation pressure of osmotic pressure or less of said aqueous solution, for example, a loose reverse osmosis membrane or an ultrafiltration membrane of a low fractionation MW grade is used. By using this separation membrane, the aqueous solution to be treated is subjected to membrane separation treatment under operation pressure of osmotic pressure or more of said aqueous solution and an untransmitted solution is recirculated to a raw solution tank during treatment and diluting water is added to said tank to hold the liquid level of the raw solution tank to a constant level. By this method, because inorg. salts are transmitted but org. valuables with a MW of 1,000 or less are not transmitted, valuables can be selectively concentrated and recovered.
    • 10. 发明专利
    • TREATMENT OF NIGHT SOIL SLUDGE
    • JPS58159899A
    • 1983-09-22
    • JP4419582
    • 1982-03-18
    • TORAY ENG CO LTD
    • OSADA TAKESHIBABA YASUO
    • C02F11/00C02F11/12
    • PURPOSE:To subject the sludge in a night soil purifying tank to concn. and volume reduction in a pretreatment to save energy in a final treatment by combining the respective stages of the 1st flocculation and solid-liquid sepn., dehydration, biological treatment, the 2nd flocculation and solid-liquid sepn., flocculation, membrane sepn. and incineration. CONSTITUTION:A flocculating agent is added to the purifying tank sludge collected in a storage tank 1 in the 1st flocculation stage 2 so as to form flocculate. The sludge is separated to the flocculate and sewage with a tilting screen device in the 1st solid- liquid sepn. stage 3; the former is dehydrated with a dehydrator in a dehydration stage 4 and the sewage is fed together with the sewage from the stage 3 to a biological treatment stage 5. The sewage treated bioligically in said stage is treated in the same way as in the stage 2 in the 2nd flocculation stage 6 to form flocculate. The flocculate is settled in the 2nd solid-liquid sepn. stage 7 and is returned to the tank 1, and the supernatant is fed to a flocculation and filtration stage 9. A flocculating agent is mixed with the sewage and the sewage is filtered in said stage; the filtrate is subjeted to a reverse osmosis treatment in a membrane sepn. stage 11 and is separaed to permeated water and concd. water. The latter is treated together with the dehydrated cake from the stage 4 in an incineration stage 12, etc.