US2685370A - Centrifugal machine for continuous operation - Google Patents

Centrifugal machine for continuous operation Download PDF

Info

Publication number
US2685370A
US2685370A US242737A US24273751A US2685370A US 2685370 A US2685370 A US 2685370A US 242737 A US242737 A US 242737A US 24273751 A US24273751 A US 24273751A US 2685370 A US2685370 A US 2685370A
Authority
US
United States
Prior art keywords
cage
shaft
chamber
pipe
funnel
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
Application number
US242737A
Other languages
English (en)
Inventor
Ruegg Ernst
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sulzer Escher Wyss AG
Original Assignee
Escher Wyss AG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Escher Wyss AG filed Critical Escher Wyss AG
Application granted granted Critical
Publication of US2685370A publication Critical patent/US2685370A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B3/00—Centrifuges with rotary bowls in which solid particles or bodies become separated by centrifugal force and simultaneous sifting or filtering
    • B04B3/02—Centrifuges with rotary bowls in which solid particles or bodies become separated by centrifugal force and simultaneous sifting or filtering discharging solid particles from the bowl by means coaxial with the bowl axis and moving to and fro, i.e. push-type centrifuges

Definitions

  • I is the cage of a push-type centrifuge.
  • This cage I is of the sieve-lter type and it is rigidly connected through a disc 2 to a driving shaft 3 constructed as a hollow shaft.
  • the driving shaft 3 has a portion widened out to form a cylinder 4.
  • a rotational movement is imparted by an electric motor 31 and a belt driving 52 to the parts I, 2, 3 and 4, which form a rotor.
  • a displaceable piston 5 Housed in the cylinder 4 is a displaceable piston 5 which engages by means of a key 51 a longitudinal groove 41 in the said cylinder, so that it is driven on rotation of the cylinder 4, while the said longitudinal slot permits axial movements of the piston 5 in relation to the cylinder
  • the piston 5 is rigidly connected by a rod 5 to the push member constructed as a push-bottom 7. Connected for rotation with this pushbottom thediameter of which is such as to provide a small clearance with respect to the cage I by which it is surrounded, is a. filling funnel 8.
  • An axially displaceable control member 52 admits oil under pressure, delivered by a pump 53 into a chamber 54, alternately to the one or other side of the piston 5 which accordingly moves continuously backwards and forwards in the cylinder I during the rotation of the cage I, imparting thereby corresponding movements to the push-bottom I and to the inlet funnel 8, so that these parts 7, 8 are moved axially in relation to the cage I.
  • the member 52 and the pump 53 are both operatively connected to a motor 55.
  • the material to be centrifuged flows out of a storage container 9 through a non-rotating feed pipe into the inlet funnel 8.
  • the said feed pipe comprises a flexible portion It and a tube II rigidly connected thereto. I8 is secured to the container 9, and the tube II leads into the distribution chamber of the machine, the said distribution chamber being externally bounded by the funnel 8.
  • This is an imperforate conical shell adapted to resist the entrance of atmospheric air.
  • a stuiiing box I2 Situated between the delivery end of the tube iI and that part of the funnel which surrounds the said end is a stuiiing box I2 which forms a gas-tight and a liquid-tight seal between the funnel 8 and the u delivery end of tube II.
  • the distribution chamber is thus substantially isolated from the atmosphere.
  • a rod I1 is fixed at one end to the push-bottom 'I so as to rotate therewith and is mounted at the other end, which is fashioned as a disc 'I2 having convex surfaces, in a housing I3 between two axial ball bearings 74.
  • the housing 'I3 is secured to an extension 'I5 of the tube II.
  • the tube II is thus forced to follow the axial movements of the rod I1 and consequently those of the push-bottom I, which is rendered possible by the flexible portion IG of the feed pipe.
  • rails I3 secured to the machine housing 131 serve as guides for the tube I I.
  • the reference numeral I4 designates chambers which serve to collect the liquid forced through the sieve of the cage I.
  • Vthe stuing box I2 separates the distribution Vcharnber in the interior of the machine, which chamber is filled with material to be centrifuged, in an air-tight manner from the atmosphere, so that no harmful ventilation can occur in this chamber.
  • the stu'ing box I2 also prevents ma- The flexible portion terial to be centrifuged from passing into a trap I5 receiving the centrifuged material.
  • an inserted structure I3 having a filter screen I'I.
  • the mass of material contained in the funnel 8 can thus be reduced and better distributed.
  • a separation or pre-elimination of liquid can be effected in the chamber bounded by the inlet funnel 8 and the inserted structure I6, as indicated in hori- Zontal chain lines in Fig. 2.
  • This liquid can iiow off through the filter screen I'I.
  • a tube 81 may extend into the said chamber for discharging the separated liquid. In this case, the outlet end of this tube 81 lies higher than the level of the material to be centrifuged which is stored in the container 9.
  • Fig. 4 shows a form of construction in which a tube 22 of the feed pipe, extending into the distribution chamber of the machine, is pivotally mounted on the machine housing at one end at 23 and is spherically fashioned at the outlet end 2t. This end separates, in conjunction with a correspondingly spherical surface of an intermediate ring 32 bearing against the inlet funnel 8, the distribution chamber of the machine in a gastight and liquid-tight manner from the atmosphere.
  • the pressing force required for the tight bearing of the said spherical surfaces is produced by a spring 25 adjustable by a nut 251.
  • This spring 25 bears at one end against the sphericallyshaped part I6 of the rod 71, which is provided with a joint 18, and at the other end against a disc “I7 fixed to the rod 11.
  • the parts I6 and 'I7 are enclosed in a housing I9 provided on the tube 22.
  • Figs. 5 and 6 show a form of construction in which the feed pipe comprises a T-shaped link pin '28, 281 and a tubular portion 29 secured to the storage container 9.
  • the vertical arm 28 of the link pin extends into the distribution chamber of the cage and the tubular portion 29 extends into the horizontal arm 281 of the link pin, there being provided at this leading-in point a stuffing box 33 sealing the interior of the feed pipe from the outside.
  • a spherical surface 32 which is intended to cooperate with a correspondingly spherically fashioned surface of an intermediate ring 34 which bears against a hooked end of the inlet funnel 8, for the purpose of providing a gas-tight and fluid-tight seal at the points of contact between the spherical surfaces.
  • the horizontal arm 281 of the link pin is pivotally mounted in two bearings 3I provided on the machine housing, so that here again the portion 28, 281 of the feed pipe is able to follow the axial relative movements of the push-bottom 1, that is, of the rod rigidly connected thereto.
  • the operation of the centrifugal machine may be adapted in other ways to the quantity of material to be centrifuged arriving from a manufacturing plant, for example by varying the number of strokes of the pusher member per unit of time.
  • the delivery volume of the hydraulic pump 53 shown in Fig. 1 and delivering the oil under pressure required for effecting the reciprocating movements of the pusher member 'i may be varied. This may be achieved, for instance, by constructing the motor 55 driving the pump 53 as a commutator motor allowing of Varying the speed of the pump.
  • a continuously operable centrifugal machine comprising a rotary driving shaft; a f0- raminous separator cage rigidly connected with said shaft; a housing enclosing said cage; a pusher member encircled by said cage and splined to said shaft so as to be shiftable in said cage in the direction of the shaft axis while turning with the shaft and cage; means for so shifting said pusher member; a flaring distributor shell connected with the pusher member so as to partake of the motions thereof and define therewith a distribution chamber isolated from the atmosphere by said shell, said chamber having an inlet on the axis of its rotation and a ⁇ peripheral discharge adjacent said cage; a nonrotating pipe opening into said inlet; a fluid tight running seal between said pipe and distributor shell; and means associated with said pipe for accommodating the axial motion of said distributor chamber while maintaining said seal.
  • a continuously operable centrifugal machine comprising a rotary driving shaft; a foraminous separator cage rigidly connected with said shaft; a housing enclosing said cage; a pusher member encircled by said cage and splined to said shaft so as to be shiftable in said cage in the direction ofthe shaft axis while turning with the shaft and cage; means for so shifting said pusher member; two spaced coaxial flaring shells connected with the pusher member so as to partake of the motions thereof and define therewith a distribution chamber separated from the atmosphere by the outer one of said shells, said chamber having an inlet on the axis of its rotation and a peripheral discharge from the annular space between the shells and adjacent said cage; a non-rotating pipe opening into said inlet; a uid tight running seal between said pipe and said outer shell; and means associated with said pipe for accommodating the axial motion of said distributing chamber while maintaining said seal.
  • a continuously operable centrifugal machine comprising a rotary driving shaft; a foraminous separator cage rigidly connected with said shaft; a housing enclosing said cage; a pusher member encircled by said cage and splined to said shaft so as to be shiftable in said cage in the direction of the shaft axis while turning with the shaft and cage; means for so shifting said pusher member; two spaced coaxial flaring shells connected with the pusher member so as to partake of the motions thereof and define therewith a distribution chamber separated from the atmosphere by the outer one of said shells, said chamber having an inlet on the axis of its rotation and a peripheral discharge from the annular space between the shells and adjacent said cage; a non-rotating pipe opening into said inlet; a fluid tight running seal between said pipe and said outer shell; means associated with said pipe for accommodating the axial motion of said distributing chamber while maintaining said seal; and a third flaring shell spaced from and encircling the first two shells and said running seal, and
  • a continuously operable centrifugal machine comprising a rotary driving shaft; a foraminous separator cage rigidly connected with said shaft; a housing enclosing said cage; a pusher member encircled by said cage and splined to said shaft so as to be shifable in said cage in the direction of the shaft axis While .turning with the shaft and cage; means for so shifting said pusher member; a daring distributor shell connected with the pusher member so as to partake of the motions thereof and define therewith a distribution chamber separated from the atmosphere by said shell, said chamber having an inlet on the axis of its rotation and a peripheral discharge adjacent said cage; a non-rotating pipe opening into said inlet; a fluid tight y running seal between said pipe and distributor shell; means associated with said pipe for accommodating the axial motion of said distributor shell while maintaining said seal; and a flaring shell spaced from and encircling said distributor shell and said running seal and connected to rotate therewith, and being arranged to intercept leakage and deliver it to

Landscapes

  • Centrifugal Separators (AREA)
US242737A 1950-09-02 1951-08-20 Centrifugal machine for continuous operation Expired - Lifetime US2685370A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CH689544X 1950-09-02

Publications (1)

Publication Number Publication Date
US2685370A true US2685370A (en) 1954-08-03

Family

ID=4529128

Family Applications (1)

Application Number Title Priority Date Filing Date
US242737A Expired - Lifetime US2685370A (en) 1950-09-02 1951-08-20 Centrifugal machine for continuous operation

Country Status (6)

Country Link
US (1) US2685370A (de)
BE (1) BE504773A (de)
CH (1) CH284392A (de)
DE (1) DE944118C (de)
FR (1) FR1055925A (de)
GB (1) GB689544A (de)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2820436A (en) * 1955-01-13 1958-01-21 Escher Wyss Ag Effecting relative displacement between pusher member and separator cage of a push-type centrifucal machine
US2845178A (en) * 1955-02-23 1958-07-29 Krauss Maffer A G Centrifugals
US2899065A (en) * 1953-05-25 1959-08-11 irving
US2991887A (en) * 1956-12-19 1961-07-11 Wirth Thomas Vibratory centrifuge
US3136722A (en) * 1961-10-18 1964-06-09 Pennsalt Chemicals Corp Pusher-type centrifuge
US3136721A (en) * 1961-03-31 1964-06-09 Pennsalt Chemicals Corp Centrifugal solids dryer
US4331482A (en) * 1979-09-11 1982-05-25 Braunschweigische Maschinenbauanstalt Continuously operating centrifuge
US5356366A (en) * 1989-04-13 1994-10-18 Werner Stahl Process for the operation of a pusher centrifuge
US20210316235A1 (en) * 2019-11-18 2021-10-14 Lg Chem, Ltd. Pressurizing centrifugal dehydrator

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE977591C (de) * 1953-12-25 1967-06-08 Krauss Maffei Ag Schleudertrommel von Schubzentrifugen
RU2746866C1 (ru) * 2020-08-11 2021-04-21 Российская Федерация, От Имени Которой Выступает Министерство Промышленности И Торговли Российской Федерации Автоматизированная центрифуга кислотоотжима для производства нитратов целлюлозы

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL7368C (de) *
US1138608A (en) * 1915-05-04 Laurent G G Dibbets Centrifugal device for filtering sugar-juices.
US1165567A (en) * 1915-01-28 1915-12-28 Thomas E Brown Art of centrifugal separation.
US1842464A (en) * 1929-02-13 1932-01-26 Albert T Otto & Sons Centrifugal separator
US2096594A (en) * 1933-05-15 1937-10-19 Federico Guillermo Sanchez Cil Continuous and automatic centrifugal separator
GB494409A (en) * 1937-06-11 1938-10-25 Gustav Ter Meer Improvements in push-type centrifugal separators
DE699927C (de) * 1939-02-18 1940-12-09 E H Gustav Ter Meer Dr Ing Dr Schubschleudereinlauf fuer Fasergut
US2232770A (en) * 1938-02-25 1941-02-25 Albert T Otto & Sons Inc Centrifugal machine
US2232769A (en) * 1937-08-26 1941-02-25 Albert T Otto & Sons Inc Double-drum centrifugal separator
US2232768A (en) * 1937-06-11 1941-02-25 Albert T Otto & Sons Inc Centrifugal separator
CH220555A (de) * 1941-05-12 1942-04-15 Ter Meer Gustav Ing Dr Zentrifuge mit in der Siebtrommel durch ein Treibmittel axial hin und her bewegtem, das ausgeschleuderte Gut einseitig aus der Trommel ausstossendem Schubboden.
US2472425A (en) * 1946-09-19 1949-06-07 Charles W Howard Pipe joint

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE69111C (de) * F. LUDLOFF in Berlin NW., Kaiserin Augusta-Allee Nr. 24 Zuflufsregler für Schleudertrommeln
DE25331C (de) * H. PAPE in Hamburg Verfahren, Schleudermaschinen für Flüssigkeiten während des Betriebes zu speisen und zu entleeren
DE214135C (de) *
FR496805A (fr) * 1918-05-27 1919-11-18 Louis Wilputte Perfectionnements aux fours à coke
DE575942C (de) * 1929-02-13 1933-05-04 Gustav Ter Meer Dr Ing In einer zylindrischen Siebtrommel beweglicher Vorschubkolben fuer das Schleudergut
BE396831A (de) * 1932-06-11 1900-01-01
BE483202A (de) * 1947-07-11

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL7368C (de) *
US1138608A (en) * 1915-05-04 Laurent G G Dibbets Centrifugal device for filtering sugar-juices.
US1165567A (en) * 1915-01-28 1915-12-28 Thomas E Brown Art of centrifugal separation.
US1842464A (en) * 1929-02-13 1932-01-26 Albert T Otto & Sons Centrifugal separator
US2096594A (en) * 1933-05-15 1937-10-19 Federico Guillermo Sanchez Cil Continuous and automatic centrifugal separator
GB494409A (en) * 1937-06-11 1938-10-25 Gustav Ter Meer Improvements in push-type centrifugal separators
US2232768A (en) * 1937-06-11 1941-02-25 Albert T Otto & Sons Inc Centrifugal separator
US2232769A (en) * 1937-08-26 1941-02-25 Albert T Otto & Sons Inc Double-drum centrifugal separator
US2232770A (en) * 1938-02-25 1941-02-25 Albert T Otto & Sons Inc Centrifugal machine
DE699927C (de) * 1939-02-18 1940-12-09 E H Gustav Ter Meer Dr Ing Dr Schubschleudereinlauf fuer Fasergut
CH220555A (de) * 1941-05-12 1942-04-15 Ter Meer Gustav Ing Dr Zentrifuge mit in der Siebtrommel durch ein Treibmittel axial hin und her bewegtem, das ausgeschleuderte Gut einseitig aus der Trommel ausstossendem Schubboden.
US2472425A (en) * 1946-09-19 1949-06-07 Charles W Howard Pipe joint

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2899065A (en) * 1953-05-25 1959-08-11 irving
US3092580A (en) * 1953-05-25 1963-06-04 Baker Perkins Inc Centrifugal machines
US2820436A (en) * 1955-01-13 1958-01-21 Escher Wyss Ag Effecting relative displacement between pusher member and separator cage of a push-type centrifucal machine
US2845178A (en) * 1955-02-23 1958-07-29 Krauss Maffer A G Centrifugals
US2991887A (en) * 1956-12-19 1961-07-11 Wirth Thomas Vibratory centrifuge
US3136721A (en) * 1961-03-31 1964-06-09 Pennsalt Chemicals Corp Centrifugal solids dryer
US3136722A (en) * 1961-10-18 1964-06-09 Pennsalt Chemicals Corp Pusher-type centrifuge
US4331482A (en) * 1979-09-11 1982-05-25 Braunschweigische Maschinenbauanstalt Continuously operating centrifuge
US5356366A (en) * 1989-04-13 1994-10-18 Werner Stahl Process for the operation of a pusher centrifuge
US20210316235A1 (en) * 2019-11-18 2021-10-14 Lg Chem, Ltd. Pressurizing centrifugal dehydrator
US11833458B2 (en) * 2019-11-18 2023-12-05 Lg Chem, Ltd. Pressurizing centrifugal dehydrator

Also Published As

Publication number Publication date
FR1055925A (fr) 1954-02-23
DE944118C (de) 1956-06-07
GB689544A (en) 1953-04-01
BE504773A (de)
CH284392A (de) 1952-07-31

Similar Documents

Publication Publication Date Title
US2685370A (en) Centrifugal machine for continuous operation
CN100491112C (zh) 压片机
US3339595A (en) Apparatus for transferring measured quantities of pulverulent material
US10562051B2 (en) Powder hopper for difficult-to-flow powders for use in thermal spraying and method making and using the same
US3030153A (en) Pneumatic conveyor system
US3070932A (en) Apparatus for filling and sealing the cartridges of two-piece capsules and the like
US2862659A (en) Centrifugal separator
US2719668A (en) Centrifugal bowl
US3729128A (en) High pressure centrifuge lubrication system
US444345A (en) And harold
US4320007A (en) Pusher-type centrifuge filters
US3385443A (en) Continuously operating centrifugal device
US2232770A (en) Centrifugal machine
US3659504A (en) Means for spacing a piston from a cylinder during operation
US943556A (en) Vacuum-pump.
US2757544A (en) Vibrating apparatus utilizing a liquid as eccentric weight means
US3288293A (en) Pressure filter
US3936037A (en) Vented gravity blender
US3221879A (en) Centrifuging apparatus
US1842464A (en) Centrifugal separator
US2997215A (en) Dispensing device with means to create a percussive effect
US3114655A (en) Centrifugal separator
US3043497A (en) Means for the support of the rotor in liquid ring rotary pumps
US3311421A (en) Device for the continuous pneumatic feeding of powdered or granular material
US3108951A (en) Filter cake washing device