| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 81 | 글리세롤 함유 첨가제의 존재 하의 광물질의 사이징 방법, 얻은 생성물 및 이의 용도 | KR1020127017545 | 2010-12-01 | KR101563044B1 | 2015-10-23 | 게인패트릭에이씨; 부리맛티아스 |
| 본발명은수성매질에서의사용과상용성인사이징된광물질을얻으면서공기사이징의효율이증가하도록글리세롤및/또는 1종이상의폴리글리세롤을포함하는사이징보조첨가제를사용하여또는첨가제비함유공기사이징과관련하여감소된비 사이징에너지를이용하여광물질을사이징하는방법에관한것이다. 본발명은또한페인트, 플라스틱, 인간또는동물소비용음식용도, 약학제제, 제지용펄프또는종이코팅에서의이러한방식으로얻은제품의용도에관한것이다. | ||||||
| 82 | 소잉 폐기물로부터 실리콘을 회수하는 방법 | KR1020107015957 | 2008-12-04 | KR1020100114032A | 2010-10-22 | 호프만파트리크 |
| 표면 에너지를 감소시키는 방식으로 실리콘 잔해(debris)를 탈산소화(deoxidizing)시키기 위하여 소잉 폐기물(sawing waste)을 처리하는 단계, 부유액(flotation liquid) 및 비산화(nonoxidizing) 부유 가스를 사용하는 부상(flotation) 방법을 상기 처리된 소잉 폐기물에 적용하는 단계, 및 상기 부유액의 표면에서 상기 실리콘 잔해를 회수(recovering)하는 단계를 포함하는 것을 특징으로 하는 소잉 폐기물로부터 실리콘 잔해를 분리 및 회수하는 방법이 제공된다.
|
||||||
| 83 | 탄소나노튜브의 선택적 분리 방법, 상기 방법으로 분리된탄소나노튜브를 포함하는 전극 및 탄소나노튜브용 올리고머분산제 | KR1020070052220 | 2007-05-29 | KR1020080104855A | 2008-12-03 | 신현진; 최재영; 최성재; 윤선미 |
| A method for separating a carbon nanotube into a metallic carbon nanotube and a semiconductive carbon nanotube selectively, a display electrode containing the metallic carbon nanotube separated by the method, and an oligomer dispersant for a carbon nanotube are provided to improve the yield of the separated metallic carbon nanotubes and semiconductive carbon nanotubes by using an oligomer dispersant. A method for separating a carbon nanotube into a metallic carbon nanotube and a semiconductive carbon nanotube selectively comprises the steps of preparing a mixture solution comprising a dispersant, a carbon nanotube and a solvent; dispersing the carbon nanotube in the mixture solution; and separating a semiconductive carbon nanotube from the mixture solution, wherein the dispersant is an oligomer comprising 2-24 repeating units comprising a head part and a tail part, the head part comprises 1-5 aromatic hetero rings, and the tail part comprises a hydrocarbon chain connected with the head part. | ||||||
| 84 | 플라스틱 용기를 재생하는 기계 | KR2019930700004 | 1991-11-09 | KR200131684Y1 | 1999-01-15 | 프레비에로,다리오 |
| PCT No. PCT/EP91/02135 Sec. 371 Date May 10, 1993 Sec. 102(e) Date May 10, 1993 PCT Filed Nov. 9, 1991 PCT Pub. No. WO92/08591 PCT Pub. Date May 29, 1992.The machine comprises a hollow rotary body (1) of large dimensions which may be loaded with the containers to be recycled, nozzles for supplying and spraying washing fluid at a predetermined temperature to the rotary body (1) for the mutual separation and washing of the containers and the initial separation of labels and bases, and mechanical impact devices (2), (21, 23) housed in the rotary body (1) and actuated by the rotation of this body so as to exert on the containers a mechanical action suitable for the mutual separation of the containers themselves, the separation of the stoppers and the completion of the washing and label and base separation operation. The rotary body (1) may have an inlet opening (5) and an outlet opening (7) for the containers to be recycled or a single inlet and outlet opening (30) so as to form a machine operating continuously or discontinuously respectively. | ||||||
| 85 | 재생흡착제로부터의 회분분리 | KR1019880000549 | 1988-01-25 | KR1019960000649B1 | 1996-01-11 | 마크시호프만; 마빈제이디트리히; 토마스피오에팅거 |
| 내용 없음. | ||||||
| 86 | Method and apparatus for separating the material to be fiberized under mechanical stress, such as materials and paper viscosity of plastic, such as plastic | JP53851397 | 1997-04-17 | JP3371397B2 | 2003-01-27 | シュネットラー，ハインツ，ライナー; ファールバッハ，ゲルハルト |
| 87 | A method and apparatus for separating the material to be fiberized under mechanical stress such as tenaciously torn difficult material and paper that is elastic, such as plastic | JP53851397 | 1997-04-17 | JP2001507636A | 2001-06-12 | シュネットラー，ハインツ，ライナー; ファールバッハ，ゲルハルト |
| (57)【要約】 本発明は、プラスチック類やゴムのような粘り強くちぎれにくい弾性を有する材料を特に紙のような材料から分離する方法、並びにこの方法を実施する装置に関する。 この方法は、分離されるべき材料の混合物を半径方向、軸方向及び接線方向の加速力に当て、細断された繊維質材料の物質流と本質的に元のままのプラスチック材料からなる別の物質流とを別々に取り出すことを特徴としている。 この方法を実施するための装置は、円筒状もしくは好ましくは多角形状のストレイナーバスケット（１）からなり、このストレイナーバスケットの外側ケーシングには孔（２）が設けられていて繊維質材料が通過できるようになっている。 このストレイナーバスケットの内側には同軸の駆動シャフト（３）が備わり、該駆動シャフトには好ましくはブレード（４）が堅く取り付けられている。 | ||||||
| 88 | Machinery for recycling plastic containers, in particular bottles | JP51815391 | 1991-11-09 | JP3057376B2 | 2000-06-26 | プレビエロ，ダリオ |
| PCT No. PCT/EP91/02135 Sec. 371 Date May 10, 1993 Sec. 102(e) Date May 10, 1993 PCT Filed Nov. 9, 1991 PCT Pub. No. WO92/08591 PCT Pub. Date May 29, 1992.The machine comprises a hollow rotary body (1) of large dimensions which may be loaded with the containers to be recycled, nozzles for supplying and spraying washing fluid at a predetermined temperature to the rotary body (1) for the mutual separation and washing of the containers and the initial separation of labels and bases, and mechanical impact devices (2), (21, 23) housed in the rotary body (1) and actuated by the rotation of this body so as to exert on the containers a mechanical action suitable for the mutual separation of the containers themselves, the separation of the stoppers and the completion of the washing and label and base separation operation. The rotary body (1) may have an inlet opening (5) and an outlet opening (7) for the containers to be recycled or a single inlet and outlet opening (30) so as to form a machine operating continuously or discontinuously respectively. | ||||||
| 89 | Waste handling | JP51373096 | 1995-10-20 | JPH10507407A | 1998-07-21 | オージング、ディルク |
| (57)【要約】 寸断された廃棄軽量物が、適当な大きさに粉砕されることによって噴射しうる材料に変換される。 銅および（または）シリカは磁性分離によって分離され、当該材料は冶金学的な炉またはセメントキルンに噴射される。 | ||||||
| 90 | Method of separating substances by flotation | JP23359587 | 1987-09-17 | JP2596941B2 | 1997-04-02 | マーティン テイラー ジョン; アンソニー ホワイト ディヴィッド |
| 91 | Solid separation method by simultaneous fragmentation and aggregation | JP13390385 | 1985-06-19 | JPH0745673B2 | 1995-05-17 | OREU TORASU |
| 92 | Process for separation of plastics by floatation | JP24376892 | 1992-09-11 | JPH05200326A | 1993-08-10 | GIYUNTAA DAIRINGERU; GERUHARUTO EEDERUMAN; BERUNHARUTO RAUTSUKUSUROO |
| PURPOSE: To separate off polyester plastics from a mixture of plastics easily by treating the mixture of plastics with an aq. alkali soln. and separating off polyester from polyvinyl chloride and other plastics by floatation. CONSTITUTION: A mixture of polyester, polyvinyl chloride and other plastics is treated with an aq. alkali soln. and the polyester is separated from polyvinyl chloride and other plastics by floatation. Wherein, polyester present in the mixture of plastics is converted into polyethylene terephthalate, polybutylene terephthalate, acid-modified polyester and/or glycol-modified polyester. Further, the proportion of polyester, polyvinyl chloride and other plastics is 1-99 wt.% of polyester, 99-1 wt.% of polyvinyl chloride and 0-98 wt.% of other plastics. COPYRIGHT: (C)1993,JPO | ||||||
| 93 | JPH0527696B2 - | JP50033086 | 1986-10-04 | JPH0527696B2 | 1993-04-22 | BEKUTORUGANOFU MURARI SURUTANOBICHI; BERIAEFU SERUGEI URADEIMIROBICHI; ABISHEFU DOZANTORE MURURANOBICHI; MARISHEFU BITARI PABUROBICHI; HAIROBA GURUZAJIRA KENZEGAJIROFUNA; SHIMU SUBETORANA PAFUROFUNA; SOROGU |
| 94 | JPH03500422A - | JP50824189 | 1989-07-27 | JPH03500422A | 1991-01-31 | |
| 95 | Sorting of coal | JP31398088 | 1988-12-14 | JPH01201396A | 1989-08-14 | ANTONIO BETSUTOORU; NETSURO PATSUSARIINI; ARUMANDO MARUKOTSUURIO |
| PURPOSE: To provide a method which enables the caking of coal normally difficult or unable to be caked, even at the time of performing its treatment using a light solvent, and also, enables improvement in selectivity and recovery property of the caking of coal by adding a specific caking mixture to a water-coal dispersion. CONSTITUTION: A ground coal material (a) is dispersed in water (b) to obtain a water- coal dispersion (A). On the other hand, one or more kinds of solvents (c) in 2 to 50 wt.% of the component (a), which is selected from light hydrocarbons each having a ≤70°C boiling point, (such as n-hexane), a nonionic oil-soluble additive (d) in 0.02 to 1 wt.% of the component (a) obtained by subjecting a phenolic fraction derived from coke-oven tar to controlled propoxylation and thereafter, if necessary, ethoxylating the propoxylated product and one or more heavy co-caking agents (e) in 0 to 3 wt.% of the component (a), which is selected from coal-derived oils each having a 200 to 400°C boiling point, the residual products of petroleum refining and mixtures thereof, are mixed to obtain a caking mixture (B); and then, the B component is added to the A component and mixed together, to obtain a caked or aggregated material consisting mainly of pure coal and an aqueous dispersion mainly contg. the inorganic solid matter. COPYRIGHT: (C)1989,JPO | ||||||
| 96 | Separation of ash from regenerated adsorbent | JP2183388 | 1988-02-01 | JPS63194702A | 1988-08-11 | MAAKU SHII HOFUMAN; MAABUIN JIEI DEIITORITSUHI; TOOMASU PII OOTEINGAA |
| 97 | JPS59501616A - | JP50301783 | 1983-09-26 | JPS59501616A | 1984-09-13 | |
| 98 | JPS59501539A - | JP50285883 | 1983-08-11 | JPS59501539A | 1984-08-30 | |
| 99 | JPS59501320A - | JP50216182 | 1982-05-27 | JPS59501320A | 1984-07-26 | |
| 100 | Treatment for ash | JP20731381 | 1981-12-22 | JPS58109127A | 1983-06-29 | ITOU HAYAMIZU; NAGAI CHIAKI |
| PURPOSE: To make effective use of coal ashes by adding water and a binder to the lime ashes captured, by a dust precipitator, adding surfactants thereto according to need, forming coarse grains contg. much coal, separating the same from fine powder contg. ashes at a high rate and recovering and using the separated coarse grains as fuel. CONSTITUTION: The coal ashes which are captured by an electrical dust precipitator 2 provided to the waste gas duct of a boiler firing finely grained coal and contains black coal ashes consisting essentially of the unburned carbon obtained in said precipitator are introduced into a separating tank 5 for unburned components, and water and heavy oil as a binder are added to the ashes and both are agitated and mixed to form coarse garins of the unburned components and the heavy oil, then the coarse grains and the fine grains of ashes are separated with a classifier 6. After the coarse grains are dehydrated with a dehydrator 7, the grains are supplied to a boiler 1 for use as fuel. The fine powder is discarded as it is or after said powder is dehydrated in a solid-liquid separator 8, the solids are utilized for raw materials for cement, etc. Surfactants are added in some cases into the tank 5 for the purpose of accelerating granulation. The separated water obtained in the dehydrator 7 and the separator 8 is removed of ammonia according to need and is then reused for control of slurry. COPYRIGHT: (C)1983,JPO&Japio | ||||||
QQ群二维码
意见反馈
意见反馈