US3398888A - Centrifuge with improved discharge assembly - Google Patents
Centrifuge with improved discharge assembly Download PDFInfo
- Publication number
- US3398888A US3398888A US573302A US57330266A US3398888A US 3398888 A US3398888 A US 3398888A US 573302 A US573302 A US 573302A US 57330266 A US57330266 A US 57330266A US 3398888 A US3398888 A US 3398888A
- Authority
- US
- United States
- Prior art keywords
- centrifuge
- panels
- bowl
- solids
- expansionable
- 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
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
- B04B1/20—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B7/00—Elements of centrifuges
- B04B7/02—Casings; Lids
- B04B7/04—Casings facilitating discharge
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
- B04B1/20—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles discharging solid particles from the bowl by a conveying screw coaxial with the bowl axis and rotating relatively to the bowl
- B04B2001/2091—Configuration of solids outlets
Definitions
- a centrifuge having a bowl rotatably mounted in a housing.
- a plurality of expansionable and contractable panels are mounted on the interior of the housing opl posite the solids discharge end. Pulsating air pressure is supplied to the panels to break up and discharge solid cake material which normally would stick to the housing.
- This invention relates to a centrifuge for separation of solids from liquid suspensions. More particularly the present invention relates to a centrifuge equipped with an improved assembly for the discharge of solids.
- centrifuges have been in use for some time which embody a rotating bowl and screw conveyer to separate a solid phase from a liquid suspension by means of centrifugal force. These centrifuges are commercially used where the solid particles have a higher density than does the liquid phase.
- Considerable difficulty has been encountered in operation of the foregoing type centrifuges when used with solids having a tendency to adhere to each other and to the discharge surfaces of the centrifuge.
- a severe problem has been encountered in separating solid thermoplastic particles from suspensions.
- a particularly acute problem has been encountered in separating polyvinyl chloride particles made by the suspension process from the suspension liquid. In one commercial centrifuge installation it was found that it was necessary to shut down the centrifuge for manual cleaning after operating periods as short as two hours.
- An object of the present invention is to provide a centrifuge having an improved assembly for the discharge of the solid phase.
- Another object of the present invention is to provide a centrifuge which can operate at sustained intervals without the necessity of shutting down for cleaning.
- An additional object of the present invention is to provide a centrifuge having means for periodically cleaning the surfaces in the solids discharge area.
- a further object of the present invention is the provision of a centrifuge having means to permit ready replacement of localized surface areas which are subject to wear from abrasive solid particles.
- a centrifuge having a housing and a bowl rotatably mounted in the housing.
- the bowl is provided with means for discharging solids at one end thereof.
- a screw conveyer is rotatably mounted inside the bowl.
- a plurality of expansionable members are provided within the housing in the solids discharge end of the centrifuge to break up the cake which normally forms at this end of the centrifuge.
- FIG. 1 is an elevational view of the centrifuge of the present invention having portions thereof broken away to show the internal structure
- FIG. 2 is a cross sectional view taken along the line 22 of FIGURE 1;
- FIG. 3 is a longitudinal sectional view taken along line 3-3 of FIGURE 1;
- FIG. 4 is an exploded view in perspective of the solids collection assembly utilized in the centrifuge of the present invention.
- FIG. 5 is an elevational perspective view of one embodiment of the expansionable members utilized in present invention.
- FIG. 6 is an elevational perspective view of a second embodiment of the expansionable members utilized in the present invention.
- FIG. 7 is a schematic diagram of the air supply system for the expansionable members.
- the centrifuge includes a housing, designated generally by the numeral 10, and a base 11 which provides support for the rotatable bowl 12 positioned within the housing.
- a hollow, rotatable screw conveyer 13 is provided within the bowl 12 and is suspended independently of the bowl by means of a rearward solid shaft 14 and forward hollow shaft 15.
- Shaft 15 is supported by bearing assembly 16 which is received in the recess 17 provided in the forward end of the interior of bowl 12.
- Bowl 12 is rotatably supported at its forward end by means of hollow shaft 18 which is supported in bearing block assembly 19 which rests on a portion of the base 11.
- the rear end of the bowl 12 is supported by hollow shaft 24) which is in turn supported by bearing block assembly 21 resting on base 11.
- the rearward shaft 14 of the screw conveyer is supported by means of a bearing assembly (not shown) within the drive gear assembly 22.
- Axial feed tube 23 is mounted on support bracket 24 and projects through the hollow forward shaft 15 to the hollow interior of the screw conveyor 13. Slurry flows from the opening 25 provided in the end of feed tube 23 through ports 26 provided in the wall of hollow screw conveyor 13.
- Pulley 27 is connected to hollow shaft 18 and rotates the bowl 12 in a counter-clockwise direction through V- belts and a drive motor (not shown).
- Screw conveyor 13 is rotated 'by means of drive shaft 14 through drive gear assembly 22 by means of a motor (not shown).
- the screw conveyor 13 and the rotating bowl 12 are rotated on their longitudinal axis in a clockwise direction as viewed from the end of the centrifuge equipped with pulley 27.
- Hollow screw conveyor 13 rotates in the same direction but at a lower r.p.m.
- the solids discharge end of the centrifuge is provided with a collector area defined by the forward end wall 33 of the housing 10 together with a bafiie plate 34 surrounding the bowl 12 and attached to the interior wall of housing 10.
- the solid discharge assembly 35 includes a plurality of interconnected support panels 36 which form an inverted U- shaped structure within the solids collector area.
- the forward wall member 37 is attached to to one side of the interconnected support panels 36 by means of bolts 38 and nuts 39;.
- a rearward wall member number 40 is attached to the opposite edges of interconnected support panels 36 by bolts 38 and nuts 39.
- Two rows of expansionable panels, designated generally by number 41, are attached to support panels 36 by means of bolts 42 as shown in FIG. 4.
- the expansionable panels 41 have an elastic covering 43.
- An air space 44 is provided within each panel 41.
- a nipple 45 connects the air space 44 to a source of compressed air conveyed to each of the panels by means of tubing 46.
- the elastic covering 43 may be of any suitable mate-rial possessing the ability to expand and contract under the influence of compressed air.
- suitable materials from which the elastic covering 43 may be fabri cated are the synthetic rubbers.
- a preferred material for elastic covering 43 is sheet polyurethane. This material has been found eminently suitable in that it is highly resistant to the abrasive action of hard solid particles. If desired the elastic covering 43 may be fabricated from thin, flexible panels of stainless steel or other suitable metal.
- expansionable panels 41 may be individual side-by-side mounted panels.
- An alternate embodiment is shown in FIGURE 6 wherein a series of single expansionable panels 41a may be utilized with each individual panel covering the width of the surface of the support panel 36.
- forward wall member 37 is covered with a coating 47 of a material which provides a non-stick surface which resists build-up of solid materials.
- Rearward wall member nu-mbef 40 has a similar coating 47 provided on its interior wall as can be seen in FIG- URE 1.
- One material which has been found suitable for the non-stick coating 47 is polytetrafluoroethylene (Teflon) which may be applied in the form of an ladhesively attached sheet, or may be sintered onto the walls by means of conventional sintering techniques. If desired the forward and rearward Wall members may be covered with a plurality of expansionable panels 41 in place of the non-sticking coating 47.
- compressed air is applied to the air space 44 within each expansionable panel by means of interconnecting tubing 46.
- High pressure compressed air is supplied through pipe 48 to filter 49, then to a pressure regulator 50, and then to an electrical pressure sequence controller, designated generally by the number 51.
- Air from the sequence controller 51 is carried by pipe number 52 through exhaust valve number 53.
- Relief valve number 54 is connected to the exhaust valve 53 and to the sequence controller by a separate line.
- Tubing 46 conducts the low pressure air to each expansionable panel carried by the support panels 36 through a network of interconnected tubing runs as shown in FIGURE 7.
- the solid material is discharged through ports 39 in the direction of the arrows where thesolid material then strikes the solids discharge assembly which surrounds the solids discharge end of the centrifuge.
- the major quantity of solids are thrown against the series of expansionable panels 41 where a gradual build-up of densely packed partcles occurs.
- air pressure is supplied to each of the panels 41 to expand the elastic covering which results in breaking off the accumulated solid layer from surface of each of the panels 41.
- the sequence controller then vents the air through exhaust valve 53.
- the panels 41 are alternately expanded and contracted on a fixed schedule when the centrifuge is operating.
- a pulsating time of /2 to 1 second has been found satisfactory for discharging polyvinyl chloride particles.
- This broken caked material then drops into the solid collection system through the opening 55 in the bottom of the centrifuge. Relatively small quantities of solid materials are thrown against the forward wall 37 and rearward wall 40. The non-stick coating 47 on each of these walls prevents any substantial quantity of the solid material from adhering to the end walls of the discharge assembly.
- one or more additional low pressure air supply lines 46 can be run from the sequence controller and connected to alternate panels. These additional supply lines are connected to a separate timer which is set to provide a pulsation cycle that is opposite to that on which the primary supply operates. This system is sometimes more effective in breaking up the caked material than is the simultaneous pulse system described hereinbefore.
- the discharge assembly used in the centrifuge of the present invention is a decided improvement over a vibrating solids discharge ring which had been used with some centrifuges heretofore.
- a single band of elastic material usually vulcanized rubber, has been used to attempt to break up the cake of solid particles in the solids discharge area of the centrifuge.
- problems were encountered in that bonding of the elastic strip was difficult to secure and also the short life of the rubber strip required frequent shutdown of the centrifuge for replacement.
- the strip was subject to the high abrasion in localized areas and it would fail before a. reasonable life expectancy was achieved.
- the present centrifuge by utilizing a plurality of individual expansionable panels permits the replacement of those panels which are subjected to erosive forces without the necessity of renewing the entire surface that is exposed to the abrasive solids.
- Continuous openating periods as long as about fourteen days to about twentyeight days have been achieved using the present lCfil'ltIlfuge for separating polyvinyl chloride from a water suspension.
- the maximum operating time for a centrifuge without the pulsating panels in PVC service was about two hours.
- a centrifuge comprising: a housing; a bowl rotatably mounted in said housing, said bowl having means for dis- 4.
- said last mentioned means includes compressed air.
- the centrifuge of claim 4 including means for simultaneous-ly expanding alternate panels and contracting intermediate panels.
Description
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US573302A US3398888A (en) | 1966-08-18 | 1966-08-18 | Centrifuge with improved discharge assembly |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US573302A US3398888A (en) | 1966-08-18 | 1966-08-18 | Centrifuge with improved discharge assembly |
Publications (1)
Publication Number | Publication Date |
---|---|
US3398888A true US3398888A (en) | 1968-08-27 |
Family
ID=24291424
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US573302A Expired - Lifetime US3398888A (en) | 1966-08-18 | 1966-08-18 | Centrifuge with improved discharge assembly |
Country Status (1)
Country | Link |
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US (1) | US3398888A (en) |
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1992005876A1 (en) * | 1990-09-27 | 1992-04-16 | Conoco Specialty Products Inc. | Method and apparatus for reduction of particles disintegration |
US5252202A (en) * | 1991-11-19 | 1993-10-12 | Daiyo Kiko Industry, Inc. | Muddy and waste water treatment device and method |
US5257968A (en) * | 1991-06-06 | 1993-11-02 | Alfa Laval Separation Inc. | Inflatable dam for a decanter centrifuge |
DE4238568A1 (en) * | 1992-11-16 | 1994-05-19 | Siteg Siebtech Gmbh | Centrifuge with filter solid particles collecting chamber surrounded by pressurised chamber - with inlet for fluidising medium minimises physical damage to the filtrate product |
US5509882A (en) * | 1994-09-12 | 1996-04-23 | Tetra Laval Holdings & Finance S.A. | Decanter centrifuge having an offset conveyor flight to aid rinsing |
US6248055B1 (en) * | 1997-04-01 | 2001-06-19 | Westfalia Separator Ag | Housing structure for use in a horizontal solid-bowl screw decanter centrifuge |
US6572524B1 (en) | 2000-07-14 | 2003-06-03 | Alfa Laval Inc. | Decanter centrifuge having a heavy phase solids baffle |
US20030228966A1 (en) * | 2000-08-31 | 2003-12-11 | Koch Richard James | Centrifuge systems and methods |
US7282019B2 (en) * | 2005-04-25 | 2007-10-16 | Edward Carl Lantz | Centrifuge with shaping of feed chamber to reduce wear |
US20090215604A1 (en) * | 2005-06-04 | 2009-08-27 | Hiller Gmbh | Helical conveyor centrifuge |
US20120010065A1 (en) * | 2008-11-28 | 2012-01-12 | Alfa Laval Corporate Ab | Decanter centrifuge with a hinged lid |
WO2015049705A1 (en) * | 2013-10-02 | 2015-04-09 | Mantovani & Vicentini S.R.L. | Centrifugal separator |
WO2015049703A1 (en) * | 2013-10-02 | 2015-04-09 | Mantovani & Vicentini S.R.L. | Centrifugal separator |
CN104624395A (en) * | 2014-12-31 | 2015-05-20 | 江苏华大离心机股份有限公司 | Horizontal centrifugal machine with scraper device |
US20160368002A1 (en) * | 2015-06-19 | 2016-12-22 | Andritz S.A.S. | Decanter centrifuge |
US20210394203A1 (en) * | 2020-06-22 | 2021-12-23 | National Oilwell Varco, L.P. | Decanter centrifuge nozzle |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2186836A (en) * | 1937-07-10 | 1940-01-09 | John P Mcglaughlin | Process and apparatus for treating materials in centrifugals |
US2324933A (en) * | 1941-05-02 | 1943-07-20 | Sharples Corp | Centrifugal separator |
US2661150A (en) * | 1947-12-17 | 1953-12-01 | Jr William G Abbott | Centrifuge |
US3105045A (en) * | 1962-01-04 | 1963-09-24 | Sharples Corp | Centrifuge discharge means |
US3326458A (en) * | 1965-05-28 | 1967-06-20 | Harold T Meryman | Container and process of storing blood |
-
1966
- 1966-08-18 US US573302A patent/US3398888A/en not_active Expired - Lifetime
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2186836A (en) * | 1937-07-10 | 1940-01-09 | John P Mcglaughlin | Process and apparatus for treating materials in centrifugals |
US2324933A (en) * | 1941-05-02 | 1943-07-20 | Sharples Corp | Centrifugal separator |
US2661150A (en) * | 1947-12-17 | 1953-12-01 | Jr William G Abbott | Centrifuge |
US3105045A (en) * | 1962-01-04 | 1963-09-24 | Sharples Corp | Centrifuge discharge means |
US3326458A (en) * | 1965-05-28 | 1967-06-20 | Harold T Meryman | Container and process of storing blood |
Cited By (28)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1992005876A1 (en) * | 1990-09-27 | 1992-04-16 | Conoco Specialty Products Inc. | Method and apparatus for reduction of particles disintegration |
US5151079A (en) * | 1990-09-27 | 1992-09-29 | Conoco Specialty Products Inc. | Method and apparatus for reduction of particle disintegration |
US5257968A (en) * | 1991-06-06 | 1993-11-02 | Alfa Laval Separation Inc. | Inflatable dam for a decanter centrifuge |
US5252202A (en) * | 1991-11-19 | 1993-10-12 | Daiyo Kiko Industry, Inc. | Muddy and waste water treatment device and method |
US5338459A (en) * | 1991-11-19 | 1994-08-16 | Daiyo Kiko Industry, Inc. | Muddy and waste water treatment method |
DE4238568A1 (en) * | 1992-11-16 | 1994-05-19 | Siteg Siebtech Gmbh | Centrifuge with filter solid particles collecting chamber surrounded by pressurised chamber - with inlet for fluidising medium minimises physical damage to the filtrate product |
US5509882A (en) * | 1994-09-12 | 1996-04-23 | Tetra Laval Holdings & Finance S.A. | Decanter centrifuge having an offset conveyor flight to aid rinsing |
US6248055B1 (en) * | 1997-04-01 | 2001-06-19 | Westfalia Separator Ag | Housing structure for use in a horizontal solid-bowl screw decanter centrifuge |
US6572524B1 (en) | 2000-07-14 | 2003-06-03 | Alfa Laval Inc. | Decanter centrifuge having a heavy phase solids baffle |
US20030228966A1 (en) * | 2000-08-31 | 2003-12-11 | Koch Richard James | Centrifuge systems and methods |
US7018326B2 (en) * | 2000-08-31 | 2006-03-28 | Varco I/P, Inc. | Centrifuge with impellers and beach feed |
US7282019B2 (en) * | 2005-04-25 | 2007-10-16 | Edward Carl Lantz | Centrifuge with shaping of feed chamber to reduce wear |
US20090215604A1 (en) * | 2005-06-04 | 2009-08-27 | Hiller Gmbh | Helical conveyor centrifuge |
US7862493B2 (en) * | 2005-06-04 | 2011-01-04 | Guenter Haider | Centrifuge for continuous separation of flowable substances of different densities having an air extraction member |
US20120010065A1 (en) * | 2008-11-28 | 2012-01-12 | Alfa Laval Corporate Ab | Decanter centrifuge with a hinged lid |
US8235882B2 (en) * | 2008-11-28 | 2012-08-07 | Alfa Laval Corporate Ab | Decanter centrifuge with a hinged lid |
US10052640B2 (en) * | 2013-10-02 | 2018-08-21 | Mantovani & Vicentini S.R.L | Centrifugal separator having one or more movable separation nets and at least one adjusting member for positioning said nets |
WO2015049705A1 (en) * | 2013-10-02 | 2015-04-09 | Mantovani & Vicentini S.R.L. | Centrifugal separator |
WO2015049703A1 (en) * | 2013-10-02 | 2015-04-09 | Mantovani & Vicentini S.R.L. | Centrifugal separator |
US20160236208A1 (en) * | 2013-10-02 | 2016-08-18 | Mantovani & Vicentini S.R.L. | Centrifugal separator |
US20160236207A1 (en) * | 2013-10-02 | 2016-08-18 | Mantovani & Vicentini S.R.L. | Centrifugal separator |
US10654049B2 (en) * | 2013-10-02 | 2020-05-19 | Mantovani & Vicentini S.R.L. | Centrifugal separator having at least a vibrating unit and one or more drum shock absorbers |
CN104624395A (en) * | 2014-12-31 | 2015-05-20 | 江苏华大离心机股份有限公司 | Horizontal centrifugal machine with scraper device |
CN104624395B (en) * | 2014-12-31 | 2016-10-12 | 江苏华大离心机制造有限公司 | Horizontal centrifuge with doctor blade device |
US9931643B2 (en) * | 2015-06-19 | 2018-04-03 | Andritz S.A.S. | Decanter centrifuge with wear-resistant accelerator inserts |
US20160368002A1 (en) * | 2015-06-19 | 2016-12-22 | Andritz S.A.S. | Decanter centrifuge |
US20210394203A1 (en) * | 2020-06-22 | 2021-12-23 | National Oilwell Varco, L.P. | Decanter centrifuge nozzle |
US11772104B2 (en) * | 2020-06-22 | 2023-10-03 | National Oilwell Varco, L.P. | Decanter centrifuge nozzle |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: GEORGIA-PACIFIC CORPORATION, 133 PEACHTREE ST., NE Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:ETHYL CORPORATION;REEL/FRAME:004245/0719 Effective date: 19831128 |
|
AS | Assignment |
Owner name: GEORGIA-PACIFIC CHEMICALS, INC., Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:GEORGIA-PACIFIC CORPORATION A CORP. OF GA;REEL/FRAME:004302/0827 Effective date: 19840827 |
|
AS | Assignment |
Owner name: GENERAL ELECTRIC CREDT CORPORATION, A NY CORP. Free format text: SECURITY INTEREST;ASSIGNOR:GEORGIA GULF CORPORATION A DE CORP.;REEL/FRAME:004346/0081 Effective date: 19841231 |
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AS | Assignment |
Owner name: NCNB NATIONAL BANK OF NORTH CAROLINA, 4151 ASHFORD Free format text: ASSIGNMENT OF ASSIGNORS INTEREST. IN SECURITY AGREEMENT DATED 12/31/86;ASSIGNOR:GENERAL ELECTRIC CREDIT CORPORATION, A N.Y. CORP.;REEL/FRAME:004625/0977 Effective date: 19861028 |
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AS | Assignment |
Owner name: GEORGIA GULF CORPORATION, A DE CORP., GEORGIA Free format text: RELEASED BY SECURED PARTY;ASSIGNOR:NCNB NATIONAL BANK OF NORTH CAROLINA;REEL/FRAME:005323/0812 Effective date: 19900427 |