WO2012161560A2 - Modern decanter - Google Patents

Modern decanter Download PDF

Info

Publication number
WO2012161560A2
WO2012161560A2 PCT/MY2012/000104 MY2012000104W WO2012161560A2 WO 2012161560 A2 WO2012161560 A2 WO 2012161560A2 MY 2012000104 W MY2012000104 W MY 2012000104W WO 2012161560 A2 WO2012161560 A2 WO 2012161560A2
Authority
WO
WIPO (PCT)
Prior art keywords
decanter
bowl
nozzles
modern
shrouds
Prior art date
Application number
PCT/MY2012/000104
Other languages
French (fr)
Other versions
WO2012161560A3 (en
Inventor
Kong @ Loh Tong Weng Lok
Original Assignee
Lok Kong Loh Tong Weng
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 Lok Kong Loh Tong Weng filed Critical Lok Kong Loh Tong Weng
Publication of WO2012161560A2 publication Critical patent/WO2012161560A2/en
Publication of WO2012161560A3 publication Critical patent/WO2012161560A3/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • C02F11/127Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering by centrifugation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/02Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles without inserted separating walls
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B1/00Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
    • B04B1/10Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl
    • B04B1/12Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl with continuous discharge
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04BCENTRIFUGES
    • B04B11/00Feeding, charging, or discharging bowls
    • B04B11/02Continuous feeding or discharging; Control arrangements therefor

Abstract

A modem decanter is different from its predecessors of prior art in that it has no scroll. The modern decanter comprises a bowl (7) and a hood (10). The modern decanter is installed upright for normal operation. The slurry (1) is fed under either dynamic or static pressure in order to achieve the designed throughput and separation efficiency. Said slurry (1) is fed through a feed pipe (1A) from top of said decanter. Said bowl (7) is cylindrical and partially perforated. The perforation is fitted with nozzles (5). Said nozzles are shrouded with shrouds (6). Due to centrifugal force, the slurry (1) is separated into solid phase (4), heavy phase (2) and light phase (3). The solid phase (4) is discharged through nozzles (5), heavy phase (2) and light phase (3) are pushed upwards in the annular spaces of concentric pipes around the feed pipe (1A) and out through their respective outlet ports. The solid phase (4) is collected by hood (10) and subsequently drops down and out via spout (9). The nozzles and shrouds are flanged. Material, used for making the said shrouds, is oil resistant and slightly springy tough to provide good seal when fitted to the bowl perforation. The structure (8) holds the decanter firmly in transit and in normal operation.

Description

Modern Decanter
Technical Field of the Invention
This invention relates to a decanter which does not have scroll for removing the solid phase. It has a partially perforated bowl and a hood shrouding the bowl. Solid phase is discharged through nozzles fitted to the perforation and collected by said hood and out via a spout. Background of the invention
In the technology of the decanting slurry, a decanter has a scroll to remove the solid phase. The decanter bowl is part cylindrical and part tapered. The scroll is a screw conveyor is also part cylindrical and part tapered. The scroll pushes the solid phase from the bigger cylindrical section of the bowl to the smaller taper end. The solid phase is discharged at the small end through a port designed for the purpose. While the light phase and heavy phase are discharged at the big end. The problems facing these types of decanter are that the wear and tear is excessive and speedy. The decanter bowl and the scroll are turning at different speeds. The scroll is spinning at much slower speed. The slurry inlet port and the scroll flights have fast and uneven wear. This has resulted in serious vibration and hence the big end and small end bearings become defective requiring renewal at fairly high frequencies. At the same time the flights have to be rebuilt and/or metal sprayed with very high wear resistant metal powder or fitted with new high resistant tiles. Similarly the inlet port has to be rebuilt. Said repair works are major and can only be done in well equipped workshop and after repair the scroll must be dynamically balanced. This major repair cannot be done on site. The workshop is normally far away from site. It therefore takes long time to complete a repair. It has therefore caused long downtimes hence affecting production quite badly. This leads to the present invention. Summary of the invention
The decanter of this invention has no scroll. The removal of solid phase is done via a partially perforated decanter bowl. The perforation is fitted with nozzles which have very high wear resistance. The wear and tear is mainly on the nozzles. The renewal of the nozzles is simple and can be easily done in the factory in remote locations. Dynamic balancing is not necessary after the renewal. Vibration of the decanter is rare. There is only one set of bearings and these bearings last much longer. There is no frequent major repair. The solid phase generated is collected by a hood shrouding the decanter bowl. The decanter is installed upright for normal operation. The solid phase collected by the hood drops down and is discharged through a spout at the lower end of the hood. Slurry inlet is at the top. At the section where the slurry splashes out into the bowl at the end of the feed pipe, said section of the bowl is not perforated.
Description of Drawings
An embodiment of the present invention will now be described by way of example only with reference to the accompanying drawings in which:
Fig. 1 (A) shows the decanter installed at an upright position for normal operation.
Fig. 1 (B) shows the cross-sectional view of the decanter.
Fig. 1 (C) is an inset depicting a nozzle fitted to the bowl body.
Description of Preferred Embodiments
Fig. 1 (A) shows the explosion view of the decanter. The slurry (1) is fed into the decanter through a feed pipe (1A) and is discharged into the bowl (7) at the end of said pipe (1A). The decanter bowl (7) is driven at high speed. This has resulted high centrifugal force. Due to the centrifugal force, the slurry (1) is separated into solid phase (4), heavy phase (2) and light phase (3). The solid phase (4) of the slurry (1) is flung out through the nozzles (5) of said bowl (7). The heavy phase (2) and light phase (3) are forced to travel upwards via the annular spaces of concentric pipes to the feed pipe (1A) and are discharged through their respective ports at the top of the decanter. This phenomenon occurs because the slurry (1) is fed into the decanter bowl (7) at some pre determined dynamic or static pressure to maintain the designed capacity of the decanter. Hood (10) collects the solid phase (4). Said solid phase (4) drops out via sprout (9) of the hood (10). Both nozzles (5) and nozzle shrouds (6) are flanged. The shrouds (6) are made of a slightly springy and tough material. The material of the nozzle shrouds is oil resistant. The shrouded nozzles (5) are tight fitted to the perforation of the bowl (7). Structure (8) holds the decanter firmly while in transit and in operation.
Herein only limited embodiments used to illustrate the best mode contemplated to carry out the invention. These embodiments are obvious to those skilled in the art. It is therefore that the invention is capable of other and different embodiments and its several details are of modifications in various aspects, none of which has departed from the invention.

Claims

THE CLAIMS DEFINING THE INVENTION ARE AS FOLLOWS:
1. A modern decanter comprising a bowl and a hood.
2. The modern decanter as claimed in claim 1 wherein said bowl is partially perforated.
3. The modern decanter as claimed in claim 1 wherein said hood shrouding said bowl, said hood collects solid phase generated by centrifugal force of said bowl spinning at high speed.
4. The modern decanter as claimed in claim 1 and 2 wherein the perforation of said bowl is fitted with nozzles.
5. The modern decanter as claimed in claim 1, 2 and 4 wherein said nozzles and nozzles shrouds are flanged, said nozzles and shrouds are fitted together in unison.
6. The modern decanter as claimed in claim 1 and 5 wherein said partially perforated bowl is fitted with unisons of nozzle and shroud.
7. The modern decanter as claimed in claim 5 and 6 wherein material of said shrouds is oil resistant and slightly springy tough to provide good seal.
8. The modern decanter as claimed in preceding claims wherein the decanter is
preferred to be installed upright for normal operation.
PCT/MY2012/000104 2011-05-24 2012-05-22 Modern decanter WO2012161560A2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
MYPI2011002298 2011-05-24
MYPI2011002298 2011-05-24

Publications (2)

Publication Number Publication Date
WO2012161560A2 true WO2012161560A2 (en) 2012-11-29
WO2012161560A3 WO2012161560A3 (en) 2013-03-28

Family

ID=47217935

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/MY2012/000104 WO2012161560A2 (en) 2011-05-24 2012-05-22 Modern decanter

Country Status (1)

Country Link
WO (1) WO2012161560A2 (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0447742B1 (en) * 1990-03-19 1994-05-18 BAKER HUGHES INC. by and through its BIRD MACHINE COMPANY DIVISION Decanter centrifuge
JPH07303463A (en) * 1994-05-12 1995-11-21 Watanabe Kikai Kogyo Kk Method for removing foreign matter of raw laver and device therefor
EP0810032A1 (en) * 1996-05-29 1997-12-03 Ecc International Limited Decanter centrifuge
US6149572A (en) * 1998-07-22 2000-11-21 Knelson; Benjamin Continuous centrifugal separator of heavier particulate materials from light particulate materials in a slurry
US20040121892A1 (en) * 2002-12-03 2004-06-24 Zonneveld Edwin John William Centrifugal separation bowl with material accelerator

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0447742B1 (en) * 1990-03-19 1994-05-18 BAKER HUGHES INC. by and through its BIRD MACHINE COMPANY DIVISION Decanter centrifuge
JPH07303463A (en) * 1994-05-12 1995-11-21 Watanabe Kikai Kogyo Kk Method for removing foreign matter of raw laver and device therefor
EP0810032A1 (en) * 1996-05-29 1997-12-03 Ecc International Limited Decanter centrifuge
US6149572A (en) * 1998-07-22 2000-11-21 Knelson; Benjamin Continuous centrifugal separator of heavier particulate materials from light particulate materials in a slurry
US20040121892A1 (en) * 2002-12-03 2004-06-24 Zonneveld Edwin John William Centrifugal separation bowl with material accelerator

Also Published As

Publication number Publication date
WO2012161560A3 (en) 2013-03-28

Similar Documents

Publication Publication Date Title
US7824459B2 (en) Centrifugal separator
US8425670B2 (en) Plant for separating oil from a gas mixture, and a method for separating oil from a gas mixture
KR102512923B1 (en) Decanter centrifuge
US20050074303A1 (en) Ejector, fine solid piece recovery apparatus and fluid conveyor
CN201701823U (en) Oil-gas separator
EP3169420B1 (en) Vertical separator for the treatment of slurry
EP2943264B1 (en) Gas desander
CN110735626A (en) pipeline type natural gas sand removing device
CN201431923Y (en) Vertical cyclone separator
EP2946836B1 (en) A centrifugal separator
WO2012161560A2 (en) Modern decanter
EP2628544B1 (en) Centrifugal separator with inlet arrangement
US20190160477A1 (en) High speed cleaning of a centrifugal separator
US10507473B2 (en) Nozzle separator bowl
NL2013662B1 (en) Centrifugal separator, cartridge unit therefor.
CN112708442B (en) Catalytic slurry oil reduced pressure distillation tower and anti-coking method thereof
CN209476484U (en) A kind of auger stripper with material acceleration function
CN203990959U (en) Seperator
CN208990993U (en) A kind of two-part horizontal decanter centrifuge
CN207170030U (en) A kind of Novel spiral discharger of spiral discharge sedimentation centrifuge
CN206951421U (en) A kind of screw feeder of centrifuge
CN207238276U (en) Horizontal type scraper centrifuger discharge nozzle anti-block apparatus
CN202508938U (en) Online desanding device of three-phase separator
CN204672457U (en) A kind of Novel spiral discharging and filtering centrifuge scraper
CN209005961U (en) A kind of decanter centrifuge housing sealing device

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 12789844

Country of ref document: EP

Kind code of ref document: A2

NENP Non-entry into the national phase

Ref country code: DE

32PN Ep: public notification in the ep bulletin as address of the adressee cannot be established

Free format text: NOTING OF LOSS OF RIGHTS PURSUANT TO RULE 112(1) EPC (EPO FORM 1205A DATED 22.04.2014)

122 Ep: pct application non-entry in european phase

Ref document number: 12789844

Country of ref document: EP

Kind code of ref document: A2