US901217A - Centrifugal disintegrator. - Google Patents
Centrifugal disintegrator. Download PDFInfo
- Publication number
- US901217A US901217A US33346806A US1906333468A US901217A US 901217 A US901217 A US 901217A US 33346806 A US33346806 A US 33346806A US 1906333468 A US1906333468 A US 1906333468A US 901217 A US901217 A US 901217A
- Authority
- US
- United States
- Prior art keywords
- disk
- shaft
- cover
- convex
- disintegrator
- 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 13
- 239000000543 intermediate Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 229910000906 Bronze Inorganic materials 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 239000010974 bronze Substances 0.000 description 1
- KUNSUQLRTQLHQQ-UHFFFAOYSA-N copper tin Chemical compound [Cu].[Sn] KUNSUQLRTQLHQQ-UHFFFAOYSA-N 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 238000011282 treatment Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
- B02C13/20—Disintegrating by mills having rotary beater elements ; Hammer mills with two or more co-operating rotors
- B02C13/205—Disintegrating by mills having rotary beater elements ; Hammer mills with two or more co-operating rotors arranged concentrically
Definitions
- Another part of :my .invention .consists i inv setting lthesstuds. or i pinsfcloser together the further they are situated "from the center.
- Figure l is a sectional relevation of the disintegrator.V Fig. la, a sectional detail view.
- Fig. 9. a plan. Fig. 3, aside elevation.
- Fig. 4 a plan view ofthe rotating con- ⁇ veX disk.
- Fig. 5 an inverted plan of the cover of the disintegrator chamber.
- the disintegrator chamber consists of a circumferential ring j provided with a lateral outlet 5 for the disintegrated material, an upper disk or cover b With central hole c for inlet of the material to be disintegrated.
- the cover is concave on the inner or under side, in which latter are suitably iXed a number of concentric rows of downwardly pointing round studs or pins CZ.
- This disk isprowided twith yconcentric studs fh intermediate of. landV clearing thefrowsr dfi the ⁇ studs or'A pins depending ⁇ from i the vrunderside ofi the chamber. cover baas ⁇ clearly,l shown in fFig. 11a.
- the -concavelconvex forinshown causes-the grainfirst to strike .against i the underside of 2 the cover b aandrto tbe# thenrthrown off on I to the rotator disk 9vg fand s to 'ffollow .a A-sinuous and :not Ia -straight course iit is I thus anorecompletely Iandi uniformlyl broughts into# contachwithf the disintegratngstuds'd.
- the rows of studs l and z are of such a diameter and are set so far apart in a. radial direction that they clear each other by about 4 millimeters more or less according to the ineness' of pulverization desired and the diameter of the fixed concave plate and the convex disk is proportional to the output of the apparatus.
- the shaft is driven in the usual manner by a pulley m which is fixed to the shaft z' by a cone sleeve 13 in two parts,
- a lubricatorwz Fig. 3 which by a pipe 0 conveys the oil to the chamber y) above the bearing 7c and surrounding the uppei end of the shaft.
- rihe chamber j is formed by expanding the upper part of the sleeve t) as shown.
- Bis the oil passes down between the bearing and the shaft f, it comes on to a convex oil shield or disk g fixed to the said shaft and is thrown off by centrifugal action into the annular oil chamber r whence it passes away by a pipe s Fig. 3, to a waste oil receptacle t whence it may be drawn o by a cock u.
- the chamber r preferably consists of a metal cup having a central hole, the bottom of the cup sloping from the central hole downwards to the walls of the cup. The upper edge of the cup is tianged enabling it to be bolted to the lower iiange l0 of the sleeve 9.
- a hopper lw provided at: its lower end with a serrated or longitudinally fluted drum a; on the shaft of which is mounted a tive speed coned pulle Y y which is suitably' driven at the desired speed.
- the hopper w is curved at its lower end to approximately fit the exterior of the tinted drum which more or less closes the hopper and it is also provided with a regulating slide or gate z having a nut l through which passes a screw 2 mounted so hopper.
- the material passes out by the lateral discharge chute 5 which may be bolted on to the ring j as shown, or formed integrally therewith and in order that none of the material shall penetrate to the bea-rings there is a packing ring or washer (i just below and surrounding the boss 7 of the convex disk y.
- a centrifugal disintegrat'or comprising a convex disk, the inclination of which is cousiderably less than thirty degrees, means tor rotating said disk, an upper stationary disk having a concavity conforming to the convexity of the first mentioned disk so that the faces of said disks are parallel, means for supporting the stationary disk a suitable distance from the convex disk, means for feeding material into the inclined space between the disks, concentrated rows ot up standing' pins on the convex disk7 and concentric rows of depending pins on the concave disk alternating with those on the convex disk, all the pins of the same vlength and the pins of the rows being closer together near the periphery of the disks than the pins of the rows near the center ⁇ whereby the fineness of pulverization of the material is increased from the center towards the periphery.
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- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Crushing And Pulverization Processes (AREA)
Description
J. B. ToUYA, JR. `GBNTI'IIIUGAL DISINTEGRA'I'OR.
APPLICATION FILED SEPT. 6
Patented ocu. 13,1908.
HHH C -mz Nomus'pzfs'ns co.. wAsmNsfraw, n. c.
J. B. TOUYA, JR. GENTRIIUGAL DISINTEGRATOR. APPLIOATION FILED SEPT. 6, 1906.
Patented Oct. 13,1908
' 2 SHEETS-SHEET 2.
i provide JEAN BAPTISTE ToUYA,JE.,.oE .TAEBEsrEANcE CENTRIF'UGAL DISIN'TEGRKTOR.
specification of Letter'sTatnt.
i Patented Oct. 13, 1908.
public, :h ave invented new :and v.useful lm` p-rovcments` ini CentrifugalDisintegrators, of
whichf the lfollowing` is `a specification.
This invention consists .in =improvements in centrifugal disintegrators suitable "for pulainggrain, ore :or other material.
. disintegnator isV ofthat :type in `which a cylindrical disintegr-ator i. chan'iber =is :used consisting of: a circumferential ring provided with outlet forfthe. disintegrated. material. il
la bottom disk'whichrisrrotated inithe chain-V ber, saidlbottom disk being provided with concentric rrows ofr rupstanding pins or studs'. v intermedi-ate. of: .and clearing theiroivs of the a foresaid depending ipins.
chambers concave i on its "lower l or @inner side the inclination being f 'considerably 2 less 'fthan i thirty degrees and therotatory diskircorre= spondmgly convex so:l thatthexopposed 'fvacesl of lsaid diskseareipanallel.
Another part of :my .invention .consists i inv setting lthesstuds. or i pinsfcloser together the further they are situated "from the center.
In order that the invention may'beunore easily understood reference .willlbeimade to the accompanying drawings which illustratey an example of disintegrator having my improvements applied thereto.
Figure l, is a sectional relevation of the disintegrator.V Fig. la, a sectional detail view. Fig. 9., a plan. Fig. 3, aside elevation. Fig. 4, a plan view ofthe rotating con-` veX disk. Fig. 5, an inverted plan of the cover of the disintegrator chamber.
The disintegrator chamber consists of a circumferential ring j provided with a lateral outlet 5 for the disintegrated material, an upper disk or cover b With central hole c for inlet of the material to be disintegrated. The cover is concave on the inner or under side, in which latter are suitably iXed a number of concentric rows of downwardly pointing round studs or pins CZ. In the chamber is arranged i a rotatable disk g xan@ upper disk: orI cover 4with central lhole ifor receiving the :material 1 to be -z disml.which isl of aconvexitycorrespondingrto the concavityiofthezunderside of the aforesaid chaniberitoponcoverrb. 'This disk isprowided twith yconcentric studs fh intermediate of. landV clearing thefrowsr dfi the `studs or'A pins depending` from i the vrunderside ofi the chamber. cover baas` clearly,l shown in fFig. 11a. In `order Sto iincrease t'hefeliiciency of =the yapparatus: thestu'clsfare by preference as shown -in Figs. '4E and f5, -set closer together ythe f-'furtherthey are situated from the center.
The degree of `concavityfisi important as it is foundthatLifsueh degree isexecuted very greatly lbeyontli that'shown on i the drawings the material under treat-ment vappears ito move outwardly intoo close contact'with the chamber cover fb andy clogging and heating iresult. @nthe.otherhandifthe angle be @less than :that shown lthe -condit-ions more nearlyiapproximate those obtaining -with the thorizontal; planeI 'oriflatf disk: type ofA machine 'heretofore :in use fin which -machine 'it Lis ffound thatfthe material passes outfto the pelripheryltoofeasilyandquickly for complete The: objecti 4of i my Vinvention isito 1 improve i i the di sintegratingaction. For fthis :purpose "l =.1nake `the itop 1 or cover :of Lthe faforesai'd disintegration to take place. The -concavelconvex forinshown causes-the grainfirst to strike .against i the underside of 2 the cover b aandrto tbe# thenrthrown off on I to the rotator disk 9vg fand s to 'ffollow .a A-sinuous and :not Ia -straight course iit is I thus anorecompletely Iandi uniformlyl broughts into# contachwithf the disintegratngstuds'd.
Mounted 'n fthe fhole v c, li-s itlre lower 1 end -of ha fchute or ffunnel v-e `which provided `withia-sieveforfgrating llheconvex disk "g which'.1s!providedwithfthe con-centricrows of upstanding studs fh is ffm-ed' on I the upper Lend o'fHawertic-alshaftii Yllhe latter revolves in a bearing c of anti-friction metal supported in a sleeve 9 and in a footstep bearing Z of phosphor bronze lixedly arranged in a bush l2 bolted to the base of the casing a. The rows of studs l and z, are of such a diameter and are set so far apart in a. radial direction that they clear each other by about 4 millimeters more or less according to the ineness' of pulverization desired and the diameter of the fixed concave plate and the convex disk is proportional to the output of the apparatus. The shaft is driven in the usual manner by a pulley m which is fixed to the shaft z' by a cone sleeve 13 in two parts,
'which sleeve is placed around the shaft 'i and is connected to the pulley m by bolts lll, screwing into the pulley. By turning the bolts 14, the pulley being held to the shaft by the set screw l5, the coned sleeve is forced into the pulley and tightly wedges the latter to the shaft e". In order to effectually lubricate the shaft` e', which suitably receives 2500 revolutions a minute7 inoi'e or less, a lubricatorwz Fig. 3, is provided which by a pipe 0 conveys the oil to the chamber y) above the bearing 7c and surrounding the uppei end of the shaft. rihe chamber j) is formed by expanding the upper part of the sleeve t) as shown. Bis the oil passes down between the bearing and the shaft f, it comes on to a convex oil shield or disk g fixed to the said shaft and is thrown off by centrifugal action into the annular oil chamber r whence it passes away by a pipe s Fig. 3, to a waste oil receptacle t whence it may be drawn o by a cock u. The chamber r preferably consists of a metal cup having a central hole, the bottom of the cup sloping from the central hole downwards to the walls of the cup. The upper edge of the cup is tianged enabling it to be bolted to the lower iiange l0 of the sleeve 9.
Above the chute c is mounted on columns fu a hopper lw provided at: its lower end with a serrated or longitudinally fluted drum a; on the shaft of which is mounted a tive speed coned pulle Y y which is suitably' driven at the desired speed. The hopper w is curved at its lower end to approximately fit the exterior of the tinted drum which more or less closes the hopper and it is also provided with a regulating slide or gate z having a nut l through which passes a screw 2 mounted so hopper. By
spectively the opening or port 16 in the wall of The said material falls down the chute e to the middle of the convex disk as to be immovable longitudi-Q nally in a bearing 3 on the outside of the; turning the screw Qthe gate a is l lifted or lowered to uncover or to cover reoe pulverized may be accurately regulated.;y
g and isg then thrown outwards by the centrifugal aci-Il tion on to the different rows of studs, one-r uni t'ormly inlverizcd. This latter action is n'rcatlv increased and rendered more perfect owing to the sloped or curved shape of the concave tixed cover t) and the convex revolving disk g. Finally the pulverizcd material reaches thc annular passage l partly incloscd by the portions towards the peripheries of the plate t and the disk g and partly by the ring j. From the passage fl the material passes out by the lateral discharge chute 5 which may be bolted on to the ring j as shown, or formed integrally therewith and in order that none of the material shall penetrate to the bea-rings there is a packing ring or washer (i just below and surrounding the boss 7 of the convex disk y.
l claim:
A centrifugal disintegrat'or comprising a convex disk, the inclination of which is cousiderably less than thirty degrees, means tor rotating said disk, an upper stationary disk having a concavity conforming to the convexity of the first mentioned disk so that the faces of said disks are parallel, means for supporting the stationary disk a suitable distance from the convex disk, means for feeding material into the inclined space between the disks, concentrated rows ot up standing' pins on the convex disk7 and concentric rows of depending pins on the concave disk alternating with those on the convex disk, all the pins of the same vlength and the pins of the rows being closer together near the periphery of the disks than the pins of the rows near the center` whereby the fineness of pulverization of the material is increased from the center towards the periphery.
In testimony whereof l have signed my name to this specification in the presence ot' two subscribing witnesses.
JEAN BAPTTWIIC TOUY. Jn. lVitnesses Lewis Bimiiirr,
ALBERT Printmrs.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US33346806A US901217A (en) | 1906-09-06 | 1906-09-06 | Centrifugal disintegrator. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US33346806A US901217A (en) | 1906-09-06 | 1906-09-06 | Centrifugal disintegrator. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US901217A true US901217A (en) | 1908-10-13 |
Family
ID=2969640
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US33346806A Expired - Lifetime US901217A (en) | 1906-09-06 | 1906-09-06 | Centrifugal disintegrator. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US901217A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2478893A (en) * | 1945-11-26 | 1949-08-16 | David O Brant | Apparatus for liquefying frozen food products |
| US3062457A (en) * | 1957-11-21 | 1962-11-06 | Willems Peter | Method and apparatus for subjecting material to cyclic stresses at high frequency |
| US4203555A (en) * | 1978-05-15 | 1980-05-20 | Dickson Thomas D Jr | Rotary foodstuff mill and milling process |
| US4422578A (en) * | 1981-09-04 | 1983-12-27 | Stratford Squire International | Rotary grain mill having means for controlling air and grain flow therethrough, and method |
| DE3707568A1 (en) * | 1987-01-06 | 1988-07-14 | Felipe Salete | METHOD FOR PRODUCING HIGH PURITY PLANT SLIM FROM PSILLI SEEDS |
| US5020732A (en) * | 1989-06-30 | 1991-06-04 | The Procter & Gamble Company | Processes for dehusking psyllium seeds |
| US5048760A (en) * | 1988-10-03 | 1991-09-17 | The Procter & Gamble Company | Process for selectively comminuting and purifying psyllium seed husk |
| US5224655A (en) * | 1988-10-03 | 1993-07-06 | The Proctor & Gamble Company | Processes for selectively comminuting and purifying psyllium seed husk |
| US5232697A (en) * | 1989-06-30 | 1993-08-03 | The Procter & Gamble Company | Processes for cleaning psyllium seeds |
-
1906
- 1906-09-06 US US33346806A patent/US901217A/en not_active Expired - Lifetime
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2478893A (en) * | 1945-11-26 | 1949-08-16 | David O Brant | Apparatus for liquefying frozen food products |
| US3062457A (en) * | 1957-11-21 | 1962-11-06 | Willems Peter | Method and apparatus for subjecting material to cyclic stresses at high frequency |
| US4203555A (en) * | 1978-05-15 | 1980-05-20 | Dickson Thomas D Jr | Rotary foodstuff mill and milling process |
| US4422578A (en) * | 1981-09-04 | 1983-12-27 | Stratford Squire International | Rotary grain mill having means for controlling air and grain flow therethrough, and method |
| US4813613A (en) * | 1987-01-01 | 1989-03-21 | Felipe Salete | Process for the obtention of high purity mucilage |
| DE3707568A1 (en) * | 1987-01-06 | 1988-07-14 | Felipe Salete | METHOD FOR PRODUCING HIGH PURITY PLANT SLIM FROM PSILLI SEEDS |
| US5048760A (en) * | 1988-10-03 | 1991-09-17 | The Procter & Gamble Company | Process for selectively comminuting and purifying psyllium seed husk |
| US5224655A (en) * | 1988-10-03 | 1993-07-06 | The Proctor & Gamble Company | Processes for selectively comminuting and purifying psyllium seed husk |
| US5020732A (en) * | 1989-06-30 | 1991-06-04 | The Procter & Gamble Company | Processes for dehusking psyllium seeds |
| US5232697A (en) * | 1989-06-30 | 1993-08-03 | The Procter & Gamble Company | Processes for cleaning psyllium seeds |
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