81 |
Separation method and production method of minute conductive material |
JP2010223167 |
2010-09-30 |
JP2012076012A |
2012-04-19 |
YAMAGE MASASHI |
PROBLEM TO BE SOLVED: To separate a minute conductive material according to the magnitude of electric resistance and inductance.SOLUTION: The method for separating the minute conductive material includes: a first separation process of synchronizingly adding an electric field and magnetic field having the same or odd multiple of frequency with each other to a first solvent to which an aggregate comprising a plurality of the minute conductive materials is added, to disperse the minute conductive material in the solvent, and recovering the first solvent according to positions after dispersing to serve as a second solvent; a separation process of synchronizingly adding the electric field and magnetic field having the same or odd multiple of frequency with each other to the first solvent to which the aggregate comprising of the plurality of the minute conductive materials is added, to disperse the minute conductive material in the solvent, and recovering the solvent according to positions after dispersing; and a multi-stage separation process of synchronizingly adding the electric field and magnetic field while making the frequencies different each time to the recovered solvent, to disperse the minute conductive material, and repeatedly carrying out the separation process of recovering the solvent according to the positions after dispersing, twice or more times. |
82 |
Treatment method and its apparatus of contaminated soil |
JP2007258775 |
2007-10-02 |
JP2008200668A |
2008-09-04 |
SHUDO GORO |
PROBLEM TO BE SOLVED: To provide a treatment method and its apparatus treating soil contaminated with organic substances in situ by washing earth particles of the contaminated soil.
SOLUTION: A plurality of metallic hollow pipes 1 with a lot of water permeating holes 3 serving also as positive and negative electrodes is set into contaminated soil G deeper than the depth of the contaminated soil to form pipe rows A for positive electrode and pipe rows B for negative electrodes, each of them facing each other. Vibration generating devices 2 are set, washing water is appropriately sprayed over the upper surface of the contaminated soil G and sufficient amount of washing water is permeated into the contaminated soil G by the vibration of the vibration generating devices 2. Then direct current is applied to the respective electrodes to apply direct current voltage causing electroendosmosis in the contaminated soil between both electrodes. The washing water is made to flow while increasing the flow speed from the positive electrode direction to negative electrode direction by the vibration of the vibration generating devices 2, contaminated pore water among the earth particles or water with contaminant dissolved therein is carried together with the washing water to wash the contaminated soil G.
COPYRIGHT: (C)2008,JPO&INPIT |
83 |
Gas-liquid separation unit |
JP3570292 |
1992-01-27 |
JP3134452B2 |
2001-02-13 |
明子 下柳田; 良二 今井 |
|
84 |
Method and apparatus for gas purification |
JP8743996 |
1996-03-15 |
JPH09248417A |
1997-09-22 |
MIZOGAMI KAZUAKI |
PROBLEM TO BE SOLVED: To provide an ultra-pure gas from which impurities are fully removed.
SOLUTION: Nitrogen gas which flows into a gas leading pipe 14 is divided to a first flow out path comprising a discharge hole 5 and the inside of a discharge pipe 15 and a second flow out path comprising a part 4'' of a discharge hole 4 and a discharge pipe 16 and flows out of respective discharge pipes 15, 16. Nitrogen gas is primarily ionized by corona discharge generated between a discharge probe and an opposed electrode 9 in a discharge chamber 3, successively secondarily ionized, and consequently impurities, such as oxygen, in the nitrogen gas are ionized to be positive ions. The impurities, e.g. oxygen, ionized to bear positive charge receive repulsion from a positive electrode 17 and at the same time receive attraction from a negative electrode 22 and mainly flow out of the discharge pipe 16 and scarcely flow out of the discharge pipe 15. Consequently, nitrogen gas with ultrahigh purity from which impurities are removed is obtained through the discharge pipe 15.
COPYRIGHT: (C)1997,JPO |
85 |
Selective light exciting purifying apparatus and method |
JP8010393 |
1993-03-15 |
JPH06262030A |
1994-09-20 |
ISHIKAWA TOSHIAKI |
PURPOSE: To efficiently separate a specific substance with high purity by providing a device detecting an ion generated by photoionization changing corresponding to the change of the frequencies of two kinds of radiant energies.
CONSTITUTION: The evaporation source in a reaction vessel is packed with Ni metal and the packed Ni metal is evaporated under heating to generate atomic beam 10. This atomic beam 10 is irradiated with dye lasers 1, 2 due to the excitation of excimer laser. Whereupon, only the objective atom in the atomic beam 10 is ionized by a two-stage exciting process and the ionization continued thereto. An ion detector is arranged in the direction vertical to the plane formed by the atomic beam 10 and pulse laser beam and, when an electric field is applied to a pair of deflection electrodes G1, G2 arranged so as to hold the atomic beam 10 therebetween to accelerate the atomic ion ionized by laser beam toward a 2G electron multiplier SEM 7, parallel ion beam is obtained to be detected as an electron pulse signal. At this time, the wavelength of pulse laser of two-stage excitation is changed.
COPYRIGHT: (C)1994,JPO&Japio |
86 |
Electric dust collector |
JP13750692 |
1992-04-13 |
JPH05285084A |
1993-11-02 |
KURODA TETSUMASA; KURODA HIROMASA |
PURPOSE: To provide an electric dust collector which is quiet with high dust attraction effect.
CONSTITUTION: A grip part 2, a dust collection section 3, a high voltage generation section 5 and an electrode of the high voltage generation section 5 are connected to an dielectric pole arranged on the side of the grip part 2 and on the side of the dust collection section 3 separately. The dust collection section 3 is charged with a high voltage to attract dust.
COPYRIGHT: (C)1993,JPO&Japio |
87 |
JPS6315009B2 - |
JP20101582 |
1982-11-16 |
JPS6315009B2 |
1988-04-02 |
UORUTAA JEI ROOZUMASU JUNIA; UORUTAA JEI ROOZUMASU |
|
88 |
JPS6084B2 - |
JP18471081 |
1981-11-18 |
JPS6084B2 |
1985-01-05 |
SUZUKI MAKOTO |
|
89 |
JPS5848220B2 - |
JP7980182 |
1982-05-12 |
JPS5848220B2 |
1983-10-27 |
UORUTAA JEI ROZUMASU |
|
90 |
Purifying apparatus for substance |
JP4856481 |
1981-03-31 |
JPS57164942A |
1982-10-09 |
OOSHIMA TOSHIO |
PURPOSE: To separate substances having magnetic moment when ionized from a substance having no magnetic moment by evaporating and ionizing a substance to be purified in a vacuum vessel and by carrying out attraction and collection while changing the concn. of impurities in the ionized substance by applying a magnetic field.
CONSTITUTION: A cylindrical vacuum vessel 1 made of stainless steel is kept at a suitable vacuum degree with a vacuum pump while introducing Ar. A substance to be purified such as Al 4 in an evaporator 3 is evaporated by heating with a heater 5, and the vapor is ionized with a pair of high frequency electrodes as ionizers 6, 6'. A magnetic field is applied to the ions with an electromagnet 7 as a magnetic field generator, and the concn. of impurities such as U and Th ions is increased in the vicinity of the field. Al with higher U and Th content and Al with lower U and Th content are collected with the 1st substance collectors 8, 8' which are a pair of electrostatic electrodes and the 2nd substance collectors 9, 9', respectifely. By repeating said separation, U and Th ions having magnetic moment are separated from Al ions having no magnetic moment.
COPYRIGHT: (C)1982,JPO&Japio |
91 |
JPS57500140A - |
JP50083581 |
1981-02-06 |
JPS57500140A |
1982-01-28 |
|
|
92 |
JPS53921B2 - |
JP7834574 |
1974-07-10 |
JPS53921B2 |
1978-01-13 |
|
|
93 |
JPS52591B2 - |
JP7975472 |
1972-08-09 |
JPS52591B2 |
1977-01-08 |
|
|
94 |
JPS5145557B1 - |
JP4579665 |
1965-07-28 |
JPS5145557B1 |
1976-12-04 |
|
|
95 |
GAS OIL SEPARATION PLANT SYSTEMS AND METHODS FOR RAG LAYER TREATMENT |
EP19705424.0 |
2019-01-08 |
EP3737733A1 |
2020-11-18 |
SOLIMAN, Mohamed; ALANAZI, Khalid; SALU, Samusideen; AL-ZAHRANI, Talai |
|
96 |
ELECTROSTATIC COALESCER WITH RESONANCE TRACKING CIRCUIT |
EP09748677.3 |
2009-11-05 |
EP2346613B1 |
2019-03-20 |
AKDIM, Mohamed, Reda; KRUIJTZER, Govert, L.; ANTSIFEROV, Pavel |
|
97 |
GAS ELECTROSTATIC COALESCER |
EP09825412 |
2009-11-05 |
EP2352596A4 |
2014-03-26 |
AKDIM MOHAMED REDA; KRUIJTZER GOVERT L; ANTSIFEROV PAVEL |
An electrostatic coalescer that includes an outer wall defining a flow path for receiving a process fluid comprising primarily a gas, a power source, a plurality of electrode plates coupled to the power source to generate an electrical field across the flow path wherein each of the plurality of electrode plates is coated with an insulation material and at least one insulating member is disposed between two adjacent electrode plates. |
98 |
ELECTROKINETIC PUMPING |
EP95940663 |
1995-11-09 |
EP0883442A4 |
1999-10-27 |
ZANZUCCHI PETER J; BURTON CHARLOTTE A; MCBRIDE STERLING E; DEMERS ROBERT |
The invention provides electrode-based pumps (803) and methods of operating such pumps. In one embodiment, the invention provides an electrode-based pump situated in a fluid channel comprising a first electrode (801A) and a second electrode (801B), wherein the first (801A) and second (801B) electrodes have a diameter from about 25 microns to about 100 microns and are spaced from about 100 microns to about 2,500 microns apart. In another embodiment, the invention provides an electrode-based pump comprising a first electrode (801A), second electrode (801B) and third electrode (801C). |
99 |
Electrostatic dust collector for use in vacuum system |
EP89113192.2 |
1989-07-19 |
EP0356684B1 |
1992-09-30 |
Saeki, Hiroshi; Ikeda, Junji; Ishimaru, Hajime |
|
100 |
Improvements in and relating to a powder recovery apparatus |
EP85304409.7 |
1985-06-20 |
EP0165815B1 |
1989-05-17 |
Frost, Ivan Ernest; Ainsworth, James William |
A powder recovery apparatus comprising a cyclone body to separate powder particles from a suspended form and a powder sieve device to separate out reusable powder, wherein the powder sieve device is positioned to the side of the cyclone body. An intermediary powder storage chamber is provided beneath the cyclone body, and powder is fed from this chamber to the powder sieve device by a transfer pump. |