US1724041A - Separator - Google Patents
Separator Download PDFInfo
- Publication number
- US1724041A US1724041A US159175A US15917527A US1724041A US 1724041 A US1724041 A US 1724041A US 159175 A US159175 A US 159175A US 15917527 A US15917527 A US 15917527A US 1724041 A US1724041 A US 1724041A
- Authority
- US
- United States
- Prior art keywords
- drum
- casing
- outlet
- tails
- inlet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000000463 material Substances 0.000 description 9
- 239000002245 particle Substances 0.000 description 6
- 239000000543 intermediate Substances 0.000 description 3
- 239000011362 coarse particle Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C3/00—Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
- B04C3/06—Construction of inlets or outlets to the vortex chamber
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B7/00—Selective separation of solid materials carried by, or dispersed in, gas currents
- B07B7/08—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force
- B07B7/086—Selective separation of solid materials carried by, or dispersed in, gas currents using centrifugal force generated by the winding course of the gas stream
Definitions
- This invention relates to certain new and useful improvementsin separators, the peculiarities of which will be hereinafter fully described and claimed.
- the object of my invention is to provide means for varying the coarseness of the tails, and therefore of the fines, delivered from a separator, so as to obtain the desired degree of fineness of the product, irrespective of the weight of the material and of the atmospheric pressure of different elevations above sea level at which the separator is operated.
- reference letters A and B designate an exhaust fan and pulverizer respectively, of any suitable make
- C the casing of a separator, shown partly in section exemplifying my invention.
- the top D has an outlet for lines with an adjustable sleeve (E), connected by the pipe F to the exhaust fan.
- the bottom G of said casing has outlets H and H for the tails which are delivered either to the hopper I of the pulverizer or elsewhere.
- a drum that is relatively large with regard to the inlet and constitutes an expansion chamber. It is preferably formed in two parts and the upper part J slidably mounted on the lower part J as shown. The upper part J is adjusted by rods K passing through the top of the casing C, or otherwise, so that the upper edge of the said drum is brought nearer to or farther from the top D of the easing as indicated by dotted lines.
- a set of spirals, or other means for producing a whirling motion of the material that enters the drum. from the pulverizer by a pipe L, under the suction of the exhaust fan.
- the drum partJ is securely mounted at the periphery of the cone M containing the spiral blades, and may be -adjustable thereon as indicated, but without leaving any opening between the drum and the cone for the passage of air or material.
- the pulverizer B is preferably of the type having a solid cage so that the material re mains therein until it is ground fine enough to be lifted through the pipe L by the suction of the exhaust fan, and given a whirling motion as it passes the spiral blades, or other means for producing that effect.
- the coarser particles tend to hug the inside of the said drum as they ascend spirally and pass over 1921' Serial No. 159,175.
- a further lowering of the upper portion J, and corresponding increase of the opening, will allow the intermediates or medium coarse particles also, to tail off; a further lowering of the upper drum part will increase the proportion of the intermediate particles passing into the tails, and thereby separate them from” the finest particles passing to the exhaust fan.
- any desired proportion of tails can be sent over the upper edge of the drum and secure any desired proportion of the fines drawn off by the exhaust fan and delivered to any suitable place.
- the outlet E is provided with a slidable collar that depends more or less below the top D and prevents the coarser particles that may strike the said top from passing out ward with the fines.
- the tails outlets are provided with slide valves 0 to cut off or regulate the flow of tails from said outlets, and also provided with air inlet valves P by which air may be admitted in desired quantities when certain materials are being operated on, the regulated air draft upward cleaning the downwardly flowing tails of the fines carried over the drum top with the coarser particles.
- a separator of the class described comprising a casing having a bottom inlet and a top outlet having an adjustable sleeve for particle-laden air subject to air suction,
- an extensible drum forming an expansion chamber communicating with said inlet and outlet respectively and consisting of two parts-the upper part being adjustable on the lower part to make a variable annular opening near the outlet between its upper edge and the top of the casing, substantially as described.
- a separator of the class described comprising a casing having a. bottom inlet and a top outlet for particle-laden air, means at the inlet for giving a whirling motion to particle-laden air, and an adjustable drum relatively large with regard to the inlet and forming an expansion chamber in the casing and adapted to form either a closed connection between the inlet and the outlet, or form a variable annular -tails opening between the top of the casing and the adjacent end of said drum,. substantially as and for the purpose described.
Landscapes
- Crushing And Pulverization Processes (AREA)
Description
mm; W, 39%., H. M. PLAISTEDY 'SEPARATOR Filed Jan. 5, 1927 Patented Ailg. 13, 1929.
UNITED STATES HAROLD M. PLAISTED, OF ST. LOUIS, MISSOURI.
SEPARATOB.
application filed January 5,
This invention relates to certain new and useful improvementsin separators, the peculiarities of which will be hereinafter fully described and claimed.
The object of my invention is to provide means for varying the coarseness of the tails, and therefore of the fines, delivered from a separator, so as to obtain the desired degree of fineness of the product, irrespective of the weight of the material and of the atmospheric pressure of different elevations above sea level at which the separator is operated.
In the accompanying drawing, reference letters A and B designate an exhaust fan and pulverizer respectively, of any suitable make, and C the casing of a separator, shown partly in section exemplifying my invention. The top D has an outlet for lines with an adjustable sleeve (E), connected by the pipe F to the exhaust fan. The bottom G of said casing has outlets H and H for the tails which are delivered either to the hopper I of the pulverizer or elsewhere.
. Within this casing is located a drum that is relatively large with regard to the inlet and constitutes an expansion chamber. It is preferably formed in two parts and the upper part J slidably mounted on the lower part J as shown. The upper part J is adjusted by rods K passing through the top of the casing C, or otherwise, so that the upper edge of the said drum is brought nearer to or farther from the top D of the easing as indicated by dotted lines.
At or near the bottom of the drum is located a set of spirals, or other means for producing a whirling motion of the material that enters the drum. from the pulverizer by a pipe L, under the suction of the exhaust fan. The drum partJ is securely mounted at the periphery of the cone M containing the spiral blades, and may be -adjustable thereon as indicated, but without leaving any opening between the drum and the cone for the passage of air or material.
The pulverizer B is preferably of the type having a solid cage so that the material re mains therein until it is ground fine enough to be lifted through the pipe L by the suction of the exhaust fan, and given a whirling motion as it passes the spiral blades, or other means for producing that effect. The coarser particles tend to hug the inside of the said drum as they ascend spirally and pass over 1921' Serial No. 159,175.
the upper edge outside of the drum and fall to the tails outlets. The intermediate and the finest particles are nearer thecenter of the drum and are drawn out the fines outlet to the exhaust fan. It has. been found by practical use, that when the drum is extended to its full height so that it practically touches the top I) of the casing as indicated by dotted lines, all of the pulverized material will pass into the fan A, because this adjustment makes a continuous closed pipe connection system to the fan without any other outlet, for the whole of the mixed material. Dropping the upper edge of the drum slightly so as to leave a small opening, will allow only coarse particles to tail off. A further lowering of the upper portion J, and corresponding increase of the opening, will allow the intermediates or medium coarse particles also, to tail off; a further lowering of the upper drum part will increase the proportion of the intermediate particles passing into the tails, and thereby separate them from" the finest particles passing to the exhaust fan. Thus it will be seen that any desired proportion of tails can be sent over the upper edge of the drum and secure any desired proportion of the fines drawn off by the exhaust fan and delivered to any suitable place. The outlet E is provided with a slidable collar that depends more or less below the top D and prevents the coarser particles that may strike the said top from passing out ward with the fines.
The tails outlets are provided with slide valves 0 to cut off or regulate the flow of tails from said outlets, and also provided with air inlet valves P by which air may be admitted in desired quantities when certain materials are being operated on, the regulated air draft upward cleaning the downwardly flowing tails of the fines carried over the drum top with the coarser particles.
Thus it will be seen that perfect control is obtained by my device over the quantity and quality of the tails and the fines, whether the materlal being separated is comparativelythe particle-laden air a whirling motion, and a" drum forming an expansion chamber mounted in said casing and communicating with said inlet and outlet respectively and having its upper edge adjustable to and from the top of the casing and thereby adapted to contact with the casing and form a closed system to deliver all the mixed material to said outlet, or to provide a variable annular opening for discharge through said opening of portions of the mixed material, substantially as described.
' 2. A separator of the class described comprising a casing having a bottom inlet and a top outlet having an adjustable sleeve for particle-laden air subject to air suction,
means at said inlet to give the particle-laden air a whirling motion, and an extensible drum forming an expansion chamber communicating with said inlet and outlet respectively and consisting of two parts-the upper part being adjustable on the lower part to make a variable annular opening near the outlet between its upper edge and the top of the casing, substantially as described.
'3. A separator of the class described comprising a casing having a. bottom inlet and a top outlet for particle-laden air, means at the inlet for giving a whirling motion to particle-laden air, and an adjustable drum relatively large with regard to the inlet and forming an expansion chamber in the casing and adapted to form either a closed connection between the inlet and the outlet, or form a variable annular -tails opening between the top of the casing and the adjacent end of said drum,. substantially as and for the purpose described.
In testimony whereof I have aflixed my signature.
HAROLD M. PLAISTED.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US159175A US1724041A (en) | 1927-01-05 | 1927-01-05 | Separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US159175A US1724041A (en) | 1927-01-05 | 1927-01-05 | Separator |
Publications (1)
Publication Number | Publication Date |
---|---|
US1724041A true US1724041A (en) | 1929-08-13 |
Family
ID=22571398
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US159175A Expired - Lifetime US1724041A (en) | 1927-01-05 | 1927-01-05 | Separator |
Country Status (1)
Country | Link |
---|---|
US (1) | US1724041A (en) |
Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2434037A (en) * | 1943-04-02 | 1948-01-06 | Babcock & Wilcox Co | Material classifier |
US2444646A (en) * | 1944-04-04 | 1948-07-06 | Giles Dee | Smelting furnace |
US2490116A (en) * | 1947-01-08 | 1949-12-06 | American Blower Corp | Separator or collector |
US2550168A (en) * | 1947-06-18 | 1951-04-24 | Ostravske Chemicke Zd Y Narodn | Mill for the fine grinding of granular materials |
US2638219A (en) * | 1950-03-13 | 1953-05-12 | Farm Production Engineers Inc | Material separating apparatus |
US2664966A (en) * | 1949-01-15 | 1954-01-05 | Raymond H Moore | Dust arrester |
US2925884A (en) * | 1956-07-13 | 1960-02-23 | Centrifix Corp | Line purifier construction |
US3092478A (en) * | 1960-05-31 | 1963-06-04 | American Air Filter Co | Tube type dust collector arrangement |
US3119379A (en) * | 1958-04-30 | 1964-01-28 | Sweeney Maxwell Patrick | Apparatus for combustion of fuels |
US3171807A (en) * | 1960-08-22 | 1965-03-02 | Neuman Entpr Ltd | Liquid separating apparatus |
US3276592A (en) * | 1963-07-16 | 1966-10-04 | George E Neuman | Separating apparatus for fluids |
US3672502A (en) * | 1970-03-27 | 1972-06-27 | Polysius Gmbh | Apparatus for purifying dust loaded waste gases |
US3791110A (en) * | 1971-06-17 | 1974-02-12 | Siemens Ag | Apparatus for producing granular solids from the gaseous phase such as by sublimation |
US3917568A (en) * | 1972-04-26 | 1975-11-04 | Siemens Ag | Rotary flow separator for fine grain particles |
EP0140769A2 (en) * | 1983-10-07 | 1985-05-08 | Creusot-Loire | Installation for treating material in a fluidised bed |
FR2559403A1 (en) * | 1984-02-10 | 1985-08-16 | Magnavac Air Systems Ltd | PARTICLE SEPARATOR, SERIES OF SUCH SEPARATORS, AND SEPARATION METHOD |
WO2020152035A1 (en) * | 2019-01-25 | 2020-07-30 | Khd Humboldt Wedag Gmbh | Rising pipe separator |
WO2021037876A1 (en) * | 2019-08-28 | 2021-03-04 | Khd Humboldt Wedag Gmbh | Cyclone with rotating rod basket |
-
1927
- 1927-01-05 US US159175A patent/US1724041A/en not_active Expired - Lifetime
Cited By (23)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2434037A (en) * | 1943-04-02 | 1948-01-06 | Babcock & Wilcox Co | Material classifier |
US2444646A (en) * | 1944-04-04 | 1948-07-06 | Giles Dee | Smelting furnace |
US2490116A (en) * | 1947-01-08 | 1949-12-06 | American Blower Corp | Separator or collector |
US2550168A (en) * | 1947-06-18 | 1951-04-24 | Ostravske Chemicke Zd Y Narodn | Mill for the fine grinding of granular materials |
US2664966A (en) * | 1949-01-15 | 1954-01-05 | Raymond H Moore | Dust arrester |
US2638219A (en) * | 1950-03-13 | 1953-05-12 | Farm Production Engineers Inc | Material separating apparatus |
US2925884A (en) * | 1956-07-13 | 1960-02-23 | Centrifix Corp | Line purifier construction |
US3119379A (en) * | 1958-04-30 | 1964-01-28 | Sweeney Maxwell Patrick | Apparatus for combustion of fuels |
US3092478A (en) * | 1960-05-31 | 1963-06-04 | American Air Filter Co | Tube type dust collector arrangement |
US3171807A (en) * | 1960-08-22 | 1965-03-02 | Neuman Entpr Ltd | Liquid separating apparatus |
US3276592A (en) * | 1963-07-16 | 1966-10-04 | George E Neuman | Separating apparatus for fluids |
US3672502A (en) * | 1970-03-27 | 1972-06-27 | Polysius Gmbh | Apparatus for purifying dust loaded waste gases |
US3791110A (en) * | 1971-06-17 | 1974-02-12 | Siemens Ag | Apparatus for producing granular solids from the gaseous phase such as by sublimation |
US3917568A (en) * | 1972-04-26 | 1975-11-04 | Siemens Ag | Rotary flow separator for fine grain particles |
EP0140769A2 (en) * | 1983-10-07 | 1985-05-08 | Creusot-Loire | Installation for treating material in a fluidised bed |
FR2555468A1 (en) * | 1983-10-07 | 1985-05-31 | Creusot Loire | DEVICE FOR PURIFYING A GAS CHARGED WITH PARTICLES |
EP0140769A3 (en) * | 1983-10-07 | 1985-06-12 | Creusot-Loire | Installation for treating material in a fluidised bed |
FR2559403A1 (en) * | 1984-02-10 | 1985-08-16 | Magnavac Air Systems Ltd | PARTICLE SEPARATOR, SERIES OF SUCH SEPARATORS, AND SEPARATION METHOD |
WO2020152035A1 (en) * | 2019-01-25 | 2020-07-30 | Khd Humboldt Wedag Gmbh | Rising pipe separator |
EP3914399A1 (en) * | 2019-01-25 | 2021-12-01 | KHD Humboldt Wedag GmbH | Rising pipe separator |
WO2021037876A1 (en) * | 2019-08-28 | 2021-03-04 | Khd Humboldt Wedag Gmbh | Cyclone with rotating rod basket |
CN114286724A (en) * | 2019-08-28 | 2022-04-05 | Khd洪保德韦达克有限公司 | Cyclone separator with rotating rod-shaped cage |
US12103047B2 (en) | 2019-08-28 | 2024-10-01 | Khd Humboldt Wedag Gmbh | Cyclone with rotating rod basket |
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