181 |
JPS621090B2 - |
JP8943580 |
1980-07-01 |
JPS621090B2 |
1987-01-12 |
KAWASHIMA YOSHIO |
|
182 |
Apparatus for separating solid particle of recirculation type fluidized bed reactor |
JP11864985 |
1985-05-31 |
JPS6150629A |
1986-03-12 |
FUORUKE ENKUSHIYUTOREEMU |
|
183 |
JPS60183048U - |
JP305585 |
1985-01-14 |
JPS60183048U |
1985-12-04 |
|
|
184 |
Heat exchanger for thermally treating powdered material by gas |
JP21883383 |
1983-11-22 |
JPS59109775A |
1984-06-25 |
JIERAARU GESUTE |
|
185 |
JPS58183254U - |
JP7896682 |
1982-05-31 |
JPS58183254U |
1983-12-06 |
|
|
186 |
JPS56164042U - |
JP6142480 |
1980-05-07 |
JPS56164042U |
1981-12-05 |
|
|
187 |
JPS5669957U - |
JP14323580 |
1980-10-07 |
JPS5669957U |
1981-06-09 |
|
|
188 |
JPS5660958U - |
JP14368879 |
1979-10-17 |
JPS5660958U |
1981-05-23 |
|
|
189 |
Multiple type axial-flow cyclone |
JP5177079 |
1979-04-26 |
JPS55142557A |
1980-11-07 |
TEJIMA KIYOMI; TSUBOI TOSHIO; KAJITANI YUKIMASA |
PURPOSE: To permit the collection of fine dust particles by a simplified structure of a device in which plural gas discharge ports provided with guiding blades to give swirling flow to dust-containing gas and a rectifying blade are provided to a dust- containing gas discharge pipe.
CONSTITUTION: In the inside of a outer cylinder 11, a separator D is provided with a boss 12 concentrically which are supported by guide blades 13 to give a swirling flow to dust-contaning gas G and supporters 14. And, the outer cylinder 11 is provided with a separating chamber 16 with a separating groove 15 and a dust-enriched gas discharging port 17 on the upflow side of the dust-containing gas G of the supporter 14. The guide blade 13, having a S(interval)/C(length) ratio of approx. 0.6W0.3 is set so as to form a swirling angle α of approx. 40W70°. Thus, sufficient swirling flow can be given to the incoming dust-containing gas and therefore sufficient centrifugal force to collect fine dust particles can be produced.
COPYRIGHT: (C)1980,JPO&Japio |
190 |
Multiple annular type axial-flow cyclone |
JP5176979 |
1979-04-26 |
JPS55142556A |
1980-11-07 |
TEJIMA KIYOMI; TSUBOI TOSHIO; KAJITANI YUKIMASA |
PURPOSE: To raise the total efficiency of dust collecting by permitting the collection even finer dust particles by using a multiple annular type axial-flow cyclone in which guide blades by which give swirl flow to gas are provided inside an outer cylinder.
CONSTITUTION: The inside of an outer cylinder 11 of a multiple annular type axial- flow cyclone is provided concentrically with a boss 12 and inner cylinders 13 and 14 and these inclusions are supported radially by guide blades 15 to give a swirling flow to dust-containing gas G, a rectifying blade 16, and discharging pipes 17 and 18 to form the first, second and third paths P1WP3. Also, a dust-enriched gas discharging port 19, separating grooves 20W22 and a separating chamber 23 are provided. Thus, when dust-containing gas is flowed into the cyclone, a swirling flow is formed by the guide blades 15 and therefore sufficient centrifugal force is produced, whereby permitting finer dust particles to be collected.
COPYRIGHT: (C)1980,JPO&Japio |
191 |
Dust collector |
JP4584179 |
1979-04-13 |
JPS55137053A |
1980-10-25 |
SUZUKI TAKESHI; MURAO MIKIO; TAKAGISHI MASAHARU; AIZAWA KIYOSHI |
PURPOSE: To separate pulverulent bodies into a cone of a lower portion of a cylinder body, whose axis is made horizontal, to decrease the interference of a spiral vortex and to improve the efficiency of the collection of the pulverulent bodies, by a method wherein gas is introduced in the tangential direction of the cylinder body, turned and exhausted in the axis direction.
CONSTITUTION: Gas containing pulverulent bodies rises in a duct 1, and is induced into a turning chamber 3 of a cylinder body 2 in the tangential direction. In this case, the gas turns without the turbulence of the current by means of a turning guide plate 10, and is exhausted from a duct 5 through a cylinder portion 4. The pulverulent bodies contained in the gas are drawn near an inwall of the cylinder body 2 by centrifugal force. The gas containing the pulverulent bodies, whose concentration is high, falls in space 14 along the inwall 8a and a collecting guide plate 13. Since a cone 8 is formed in a shape that its lower portion becomes narrower, the speed of a fall is increased, and the pulverulent bodies drop into a collecting cylinder 9 by downward inertia force and are discharged.
COPYRIGHT: (C)1980,JPO&Japio |
192 |
JPS5511389B2 - |
JP5215578 |
1978-04-30 |
JPS5511389B2 |
1980-03-25 |
|
|
193 |
JPS544106B2 - |
JP4206974 |
1974-04-15 |
JPS544106B2 |
1979-03-02 |
|
|
194 |
Side portion outlet type cyclone separating pipe and eddy current cenerator and air purifier |
JP5215578 |
1978-04-30 |
JPS5415575A |
1979-02-05 |
BURUUSU EMU SARIBUAN; ANRI EMU KARUZUA |
|
195 |
Air cleaner for turbine engine |
JP14702377 |
1977-12-07 |
JPS53107784A |
1978-09-20 |
SEDORITSUKU SAN; CHIYAARUZU JIEE ROOCHI |
|
196 |
JPS5223419B2 - |
JP4837173 |
1973-04-26 |
JPS5223419B2 |
1977-06-24 |
|
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197 |
JPS508167A - |
JP4206974 |
1974-04-15 |
JPS508167A |
1975-01-28 |
|
|
198 |
JPS49105267A - |
JP1687873 |
1973-02-09 |
JPS49105267A |
1974-10-04 |
|
|
199 |
JPS4954965A - |
JP4837173 |
1973-04-26 |
JPS4954965A |
1974-05-28 |
|
|
200 |
JPS4430607Y1 - |
JP431769 |
1969-01-20 |
JPS4430607Y1 |
1969-12-17 |
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