WO2007093015A1 - Clarifier - Google Patents
Clarifier Download PDFInfo
- Publication number
- WO2007093015A1 WO2007093015A1 PCT/AU2007/000180 AU2007000180W WO2007093015A1 WO 2007093015 A1 WO2007093015 A1 WO 2007093015A1 AU 2007000180 W AU2007000180 W AU 2007000180W WO 2007093015 A1 WO2007093015 A1 WO 2007093015A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- juice
- clarifier
- flow
- mud
- floaters
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B20/00—Purification of sugar juices
- C13B20/16—Purification of sugar juices by physical means, e.g. osmosis or filtration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0087—Settling tanks provided with means for ensuring a special flow pattern, e.g. even inflow or outflow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/02—Settling tanks with single outlets for the separated liquid
- B01D21/04—Settling tanks with single outlets for the separated liquid with moving scrapers
- B01D21/06—Settling tanks with single outlets for the separated liquid with moving scrapers with rotating scrapers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/24—Feed or discharge mechanisms for settling tanks
- B01D21/2405—Feed mechanisms for settling tanks
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/24—Feed or discharge mechanisms for settling tanks
- B01D21/2427—The feed or discharge opening located at a distant position from the side walls
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/24—Feed or discharge mechanisms for settling tanks
- B01D21/2433—Discharge mechanisms for floating particles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/24—Feed or discharge mechanisms for settling tanks
- B01D21/2444—Discharge mechanisms for the classified liquid
Definitions
- THIS INVENTION relates to clarifers and in particular but not limited to a clarifier for sugar cane juice.
- Sugar cane juice is usually passed through a clarifier in an effort to remove "mud” and so called “floaters” from the juice.
- Juice extracted from sugar cane contains impurities including mud and fine fibre particles which should be removed to produce a high quality sugar for human consumption.
- juice clarifers are used to remove most of these impurities. This separation is achieved with the aid of a flocculent which ties the minute impurities into bundles called flocks which, because of their increased mass, sink to the bottom of the clarifier onto trays or tray type units where they are removed by scrapers.
- floaters which are fine cane fibre particles called "bagacillo" and these along with small mud particles may remain entrained in the clarified juice and flow to the take off troughs therefore reducing the quality of the clarified juice.
- bagacillo fine cane fibre particles
- the object of the present invention is to provide a clarifier which forces the unclarified juice to flow substantially horizontally in a maximum depth column to slow its horizontal flow and allow flocculated mud particles to drop out of this column early, to the bottom of the clarifier for removal and the floaters and gas particles with adhering mud and bagacillo particles to rise out of this column to the surface of the juice for removal as well. Both impurities are separated from the clarified juice.
- the clarified juice flows through a perforated, partitioned or slotted central cone to forcefully spread out the vertical depth of the juice flow by restricting the flow to decrease its horizontal flow rate to allow maximum time for the mud particles and floaters to separate from this flowing body of juice and therefore increase the capacity of the clarifier.
- the invention resides in a clarifier where flocculated relatively unclarified liquid enters the clarifier at and clarified liquid is drawn off through an outlet pipe the flow being controlled by having an intake edge at depth so there is a annular downward plug flow before cross flow commences.
- the present invention resides in a juice clarifier including a generally horizontal juice flow passage at depth across the clarifier from a entry to an exit, the exit having slow flow means to limit the flow of unclarified juice from the entry along the horizontal flow passage way, the entry juice having relatively heavy flocculated mud particles entrained therein and relatively light floaters entrained therein, the horizontal flow path is sufficiently slow as to enable floaters to move to the surface and flocculated mud particles to sink to the bottom to provide a relatively pure clarified juice at a take off.
- a rotary shaft clarifier driving a bottom scraper assembly for removal of mud sediment from the clarifier and a scraper used to remove floating particles which accumulate at the sides of the clarifier
- the clarifier having a sedimentation tank, which has a conical base section and a mud outlet section for discharge of mud settling on the insides of the conical base, the insides of the conical base being progressively scraped by scraper blades of the scraper assembly as it moves around the bottom of the tank
- relatively clarified juice passes through a perforated take off at a distance between a vertical intake having a lower intake edge defining a depth of commencement of cross flow and the take off, the distance between the intake edge and the take off being so chosen and arranged along the accompanying flow rate so that the mud being removed by sedimentation and the floating particles removed by flotation is optimised, the distance between an intake edge and the take off and the depth of the intake are selected so that the flow rate optimises the clarification.
- juice is caused to flow across the bottom of the intake edge generally horizontally at depth showing a generally horizontal flow albeit slightly upward toward the take off, the flow overall being designed to cause circulation at adjacent and above the intake edge to promote movement of floaters to a region adjacent the periphery of the clarifier.
- flow from the intake edge is uniform at about 5 mm/sec due to a feed launder at the entry to the clarifier.
- the launder includes a perforated plate with holes to allow passage of larger mud particles and to provide uniform or "plug" flow within the inlet down to the intake edge.
- the entry juice follows an initial substantially vertical plug flow downward into the clarifier.
- the relatively unclarified juice enters either from a centre feed cylinder/cone, or preferably, an outside feed ring (both of which may be perforated, partitioned or slotted to increase the depth of the horizontally flowing juice column).
- clarified juice to exit, preferably, though a perforated, partitioned or slotted central take off cylinder/cone or through a perforated, partitioned outer ring.
- a perforated, partitioned or slotted central take off cylinder/cone or through a perforated, partitioned outer ring.
- a juice flow is forced to spread up and/or down as it travels from a horizontal entry point at depth to an exit cylinder/inverted cone or outer ring, to decrease its horizontal speed and so increase the time required for separation of flocculated mud particles and floaters.
- perforated, partitioned or slotted entry and/or perforated partitioned or slotted exit cylinder/cone or outer ring is dimensioned and chosen so as to spread out the vertical depth of the horizontal juice flow to forcefully slow its cross flow rate.
- the entry should be an outer feed ring to minimise the downward flow rate of an initial vertical flow of incoming flocculated juice, to allow maximum separation of mud particles prior to the horizontal flow.
- clarifier has a base
- the base of the clarifier should be a cone with an angle downward towards the centre of at least 20 degrees to the horizontal to improve mud removal and increase mud compaction, (heavy muds) for minimum juice content in the mud being separated from the juice.
- flow across the clarifier promotes circulation adjacent the inlet to cause a low or zero flow region for collection of floaters.
- This circulation also preferably, provides an upflow to aid movement of floaters to the region for collection of floaters.
- Downward flow through the inlet is purposely set low, at about 5mm/sec to promote uniform slow velocity flow across the clarifier and thereby promote separation of floaters and mud.
- Figure 1 is a schematic sectional drawing through a clarifier according to the present invention
- FIG 2 is drawing similar to Figure 1 but illustrated the flow process of juice through the clarifier.
- Figure 3 is a computational fluid dynamics (CFD) model of a typical clarifier operation.
- a rotary shaft 13 is located in the centre of the clarifier and drives a bottom scraper assembly 14 for removal of mud sediment from the clarifier and a scraper 15 used to remove floating particles which accumulate at the sides of the clarifier as will be described below.
- the shaft 13 rotates at approximately 3 revolutions per hour.
- the clarifier includes a sedimentation tank shown generally at 16 which has a conical base section 17 and a mud outlet section at 18 mud settling on the insides of the conical surface 17 are progressively scraped from that surface by scraper blades 19, 20, 21 , 22, 23 and 24 as the scraper assembly 14 moves around the bottom of the tank 16.
- Relatively clarified juice passes through a perforated take off cone or cylinder 25 and the distance between an intake edge 26 and the perforated take off 25 is so chosen and arranged along with the dimensions of the perforations and the accompanying slow rate so that the mud is removed by sedimentation and the floating particles removed by flotation is optimised.
- the flow from feed launder 32 is uniform at about 5 mm/sec due to the constructions of the feed launder shown in inset Figure 2B.
- the launder 32 induces a perforated plate 33 with holes of about 10 mm or so to allow passage of larger mud particles. This arrangement provides uniform or "plug" flow within the inlet down to edge 26.
- FIG. 3 there is illustrated a CFD model of a 9750mm diameter clarifier with a flow rate of about 11 ,000 tonnes of juice per day.
- the mud is depicted by the closely spaced lines at 34.
- the velocity in region 36 is about 5mm/sec and the highest velocity is about 10mm/sec in the region 37.
- Velocity in the region 30 is down to zero. Velocities are shown across the drawing.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2007215398A AU2007215398B2 (en) | 2006-02-17 | 2007-02-19 | Clarifier |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2006900794A AU2006900794A0 (en) | 2006-02-17 | Clarifier | |
AU2006900794 | 2006-02-17 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2007093015A1 true WO2007093015A1 (en) | 2007-08-23 |
Family
ID=38371128
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/AU2007/000180 WO2007093015A1 (en) | 2006-02-17 | 2007-02-19 | Clarifier |
Country Status (1)
Country | Link |
---|---|
WO (1) | WO2007093015A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102719568A (en) * | 2012-05-14 | 2012-10-10 | 广西华蓝设计(集团)有限公司 | Cane juice clearing method and equipment |
WO2013111062A1 (en) * | 2012-01-24 | 2013-08-01 | Tongaat Hulett Limited | Integrated clarifier and flash tank |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2395057A1 (en) * | 1977-06-22 | 1979-01-19 | Guillaume Jean Paul | Decanter for purifying water contg. particulate materials - incorporates scraper which can be lifted clear of deposited mud, facilitating starting after prolonged stoppage |
AU2999077A (en) * | 1976-10-29 | 1979-05-03 | Bateman E L Ltd | Separation of suspended solids from liquids |
SU751833A1 (en) * | 1978-05-31 | 1980-07-30 | Ордена Трудового Красного Знамени 2-Й Им. Петровского Сахарный Завод | Settler for juices of beet-sugar production |
-
2007
- 2007-02-19 WO PCT/AU2007/000180 patent/WO2007093015A1/en active Application Filing
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU2999077A (en) * | 1976-10-29 | 1979-05-03 | Bateman E L Ltd | Separation of suspended solids from liquids |
FR2395057A1 (en) * | 1977-06-22 | 1979-01-19 | Guillaume Jean Paul | Decanter for purifying water contg. particulate materials - incorporates scraper which can be lifted clear of deposited mud, facilitating starting after prolonged stoppage |
SU751833A1 (en) * | 1978-05-31 | 1980-07-30 | Ордена Трудового Красного Знамени 2-Й Им. Петровского Сахарный Завод | Settler for juices of beet-sugar production |
Non-Patent Citations (4)
Title |
---|
DATABASE WPI Week 197810, Derwent World Patents Index; Class D15, AN 1978-17716A * |
DATABASE WPI Week 197913, Derwent World Patents Index; Class D17, AN 1979-24249B * |
DATABASE WPI Week 198015, Derwent World Patents Index; Class D17, AN 1980-26679D * |
PERRY R.H. AND GREEN D.W.: "Perry's Chemical Engineers Handbook", 1997, MCGRAW-HILL, NEW YORK, pages: 18 - 73 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013111062A1 (en) * | 2012-01-24 | 2013-08-01 | Tongaat Hulett Limited | Integrated clarifier and flash tank |
CN102719568A (en) * | 2012-05-14 | 2012-10-10 | 广西华蓝设计(集团)有限公司 | Cane juice clearing method and equipment |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP4696646B2 (en) | Sedimentation tank | |
AU2012296191B2 (en) | Deaeration apparatus and method | |
JP4774491B2 (en) | Solid-liquid separation system | |
AU2009246040A1 (en) | Apparatus and method for mechanical deaeration | |
JP5393065B2 (en) | Levitation separator | |
JP4470486B2 (en) | Sedimentation tank | |
JP5497873B2 (en) | Levitation separator | |
US20090039003A1 (en) | Single-Cell Mechanical Flotation System | |
WO2007093015A1 (en) | Clarifier | |
AU2007215398B2 (en) | Clarifier | |
AU2008230369A1 (en) | Clarifier | |
JP4825850B2 (en) | Floating separator, rectifier, and split cell for rectifier | |
AU2012213922B2 (en) | Clarifier | |
KR20050009976A (en) | Method and device for flocculating setting | |
WO2000012192A1 (en) | Apparatus for the separation of solids and liquids | |
JPH0663321A (en) | Inclined plate type settling chamber | |
JP5886518B2 (en) | Levitation separator | |
US3953328A (en) | Separation of sludge | |
JP3882464B2 (en) | Sedimentation tank | |
JP5697920B2 (en) | Levitation separator | |
KR100491353B1 (en) | liquid-solid seperator | |
KR101465718B1 (en) | Ballast water supply system and ballast water supply method | |
JP5524775B2 (en) | Levitation separator | |
RU2286827C1 (en) | Vertical settler for washing water | |
SU912208A1 (en) | Thickener |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
WWE | Wipo information: entry into national phase |
Ref document number: 2007215398 Country of ref document: AU |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
DPE2 | Request for preliminary examination filed before expiration of 19th month from priority date (pct application filed from 20040101) | ||
ENP | Entry into the national phase |
Ref document number: 2007215398 Country of ref document: AU Date of ref document: 20070219 Kind code of ref document: A |
|
WWP | Wipo information: published in national office |
Ref document number: 2007215398 Country of ref document: AU |
|
WWE | Wipo information: entry into national phase |
Ref document number: 12008501874 Country of ref document: PH |
|
WWE | Wipo information: entry into national phase |
Ref document number: 7011/DELNP/2008 Country of ref document: IN |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
122 | Ep: pct application non-entry in european phase |
Ref document number: 07701511 Country of ref document: EP Kind code of ref document: A1 |