EP0707078A1 - Nouveau procédé de déplacement de jus de cane - Google Patents
Nouveau procédé de déplacement de jus de cane Download PDFInfo
- Publication number
- EP0707078A1 EP0707078A1 EP94402832A EP94402832A EP0707078A1 EP 0707078 A1 EP0707078 A1 EP 0707078A1 EP 94402832 A EP94402832 A EP 94402832A EP 94402832 A EP94402832 A EP 94402832A EP 0707078 A1 EP0707078 A1 EP 0707078A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- juice
- cane
- extraction
- displacement
- stage
- 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.)
- Granted
Links
- 238000006073 displacement reaction Methods 0.000 title claims abstract description 67
- 238000000034 method Methods 0.000 title claims abstract description 40
- 235000011389 fruit/vegetable juice Nutrition 0.000 claims abstract description 149
- 238000000605 extraction Methods 0.000 claims abstract description 32
- 239000007788 liquid Substances 0.000 claims abstract description 8
- 238000005056 compaction Methods 0.000 claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 230000002706 hydrostatic effect Effects 0.000 claims abstract description 6
- 239000000203 mixture Substances 0.000 claims abstract description 6
- 239000007787 solid Substances 0.000 claims abstract description 6
- 238000005325 percolation Methods 0.000 claims abstract description 5
- 241000609240 Ambelania acida Species 0.000 claims description 15
- 239000010905 bagasse Substances 0.000 claims description 15
- 238000003801 milling Methods 0.000 claims description 14
- 238000009792 diffusion process Methods 0.000 claims description 11
- 238000002386 leaching Methods 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 7
- 239000002002 slurry Substances 0.000 claims description 5
- 235000016068 Berberis vulgaris Nutrition 0.000 claims description 2
- 241000335053 Beta vulgaris Species 0.000 claims description 2
- 238000012423 maintenance Methods 0.000 claims description 2
- 241000219310 Beta vulgaris subsp. vulgaris Species 0.000 claims 1
- 235000021536 Sugar beet Nutrition 0.000 claims 1
- 230000001771 impaired effect Effects 0.000 claims 1
- 230000035699 permeability Effects 0.000 claims 1
- 239000011800 void material Substances 0.000 abstract description 6
- 240000000111 Saccharum officinarum Species 0.000 abstract description 4
- 235000007201 Saccharum officinarum Nutrition 0.000 abstract description 4
- 238000000926 separation method Methods 0.000 abstract description 4
- 238000011049 filling Methods 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000002994 raw material Substances 0.000 abstract description 3
- 239000000835 fiber Substances 0.000 description 11
- 238000005213 imbibition Methods 0.000 description 11
- 238000010586 diagram Methods 0.000 description 10
- 238000002156 mixing Methods 0.000 description 8
- 230000005484 gravity Effects 0.000 description 5
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 4
- 229930006000 Sucrose Natural products 0.000 description 4
- 229960004793 sucrose Drugs 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 2
- 238000013459 approach Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 229910052709 silver Inorganic materials 0.000 description 2
- 239000004332 silver Substances 0.000 description 2
- CZMRCDWAGMRECN-UHFFFAOYSA-N Rohrzucker Natural products OCC1OC(CO)(OC2OC(CO)C(O)C(O)C2O)C(O)C1O CZMRCDWAGMRECN-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000001413 cellular effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000003113 dilution method Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B10/00—Production of sugar juices
- C13B10/02—Expressing juice from sugar cane or similar material, e.g. sorghum saccharatum
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B10/00—Production of sugar juices
- C13B10/02—Expressing juice from sugar cane or similar material, e.g. sorghum saccharatum
- C13B10/04—Expressing juice from sugar cane or similar material, e.g. sorghum saccharatum combined with imbibition
Definitions
- the first step is to open the juice containing cells so that the extractable juice of cane be readily available for leaching or displacement.
- 80 to 84 % of the extractable juice % cane (1) can be extracted by dry pressure in a mill. Sugar (Pol) extraction is from 60 to 80 %. For higher extraction, imbibition have to be resorted to. The aim of imbibition is to dilute the extractable juice of cane before the final juice extraction by pressure.
- Extractable juice % cane 100-1.25 F If fiber % cane (F) is 16 then extractable juice % cane is 80 %
- n° 1 mill bagasse is processed in a counter-current multistage dilution process. In each stage, two separate operations take place :
- stage efficiency in diffusion is not any better than in milling.
- the number of stages used which should be between 4 and 7 (depending on the imbibition rate) assuming 100 % efficient mixing, is between 15 to 18 (so that the stage efficiency is between 4/15 (26.7 %) to 7/18 (38.9 %)
- the bulk density may vary from 250 to 350 Kg/cubic meter.
- the average bulk density (counted on cane only) is between 500 to 600 Kg cubic meter. Which means that the average apparent volume occupied by one ton of cane must be between 1.67 to 2 cubic meters. Deducting the no void volume of cane, this leaves a void volume of between 0.78 to 1.11 cubic meter. The filling of this void volume of with 1.05 density juice will require 819 Kg to 1.655 Kg of juice.
- the object of the present patent is to make the cane juice displacement process efficient by resorting to "meichage" in a continuous cane juice extraction equipment.
- the target of 4 brix of juice in the final megasse (corresponding to a Pol extraction rate of 98 %, assuming a final dewatering giving a juice content of the bagasse of 0.64 F) is reached in three stages.
- the meichage juice (14 F) will be supplied by the drainage juice with a mixed brix of 5.7
- the dewatering mill juice (5.36 F) will be used as displacement juice, followed by imbibition water 2 F
- the brix of the displaced juice (7.36 F) will be 6.22
- a conventional horizontal drag type conveyor can be used to move the prepared cane delivered by the shredder to the dewatering mill.
- the speed of the conveyor (approximately 20 meter/minute) is set according to the cane flow so that a layer of about 0,3 meter is moved along, over the perforated bottom (1) of the conveyor.
- the conveyor has a closed double bottom (2) with compartments and piping to comply with the flow diagram in each of the 3 stages.
- the megasse is discharged from the last section of the displacement conveyor into the chute (9) feeding the preextractor (PE)
- the preextractor consists in conventional 4 roller mill from which the trash plate and the delivery roll have been removed. It is a tilted 3 roller mill set to remove half of the juice content (6 F) of the megasse.
- the bagasse coming out of the preextractor is conveyed by a closed chute (Meinecke chute) (C) to the bottom of the conventional bagasse elevator (E) feeding the (Donelly) chute of the final dewatering mill (DWM) which is a conventional 4 roller mill receiving the usual juice content (3 F) consisting, in a conventional milling tandem of the juice content (IF) of the second last mill bagasse and of the imbibition water (2 F) added in front of the last mill.
- C closed chute
- E bagasse elevator
- DWM final dewatering mill
- the dewatering juice coming from the preextractor (3 F) and the final dewatering mill (2.36 F) are pumped at the rate of 5.36 F to the displacement juice trough (5) of the third stage by pump (10).
- displacement juice from the third stage is pumped from tank 8 by pump (10) to the displacement juice trough (5) of the second stage.
- Displacement juice for n° 1 stage is pumped from 2nd stage tank (8) by pump (10) to N° 1 stage displacement juice trough.
- the juice extracted from the plant overflows from receiving tank (8) of the first stage into a pump feed tank (11) from which it is pumped at the rate of 6.36 F as mixed juice to the process.
- the level of juice in the receiving tank (8) in each stage must be at least 2 meters, and preferably between 3 to 4 meters lower than the level of juice in the conveyor (top of the cane bed).
- the conventional drag type conveyor can be used for juice extraction by the displacement process, only up to a capacity of 5/6000 tons of cane per day, because of the following limitations :
- the displacement process can only be performed efficiently when the juice content of the megasse is at least 20 times the fiber content of the cane - which means that the fiber content of the megasse must be less than 1/20 or 5 %.
- megasse has the hydrodynamic characteristics of a liquid.
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Non-Alcoholic Beverages (AREA)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU74195/94A AU679255B2 (en) | 1994-09-26 | 1994-09-26 | New cane juice displacement process |
| AU7419594 | 1994-09-26 | ||
| AU74195/94 | 1994-09-26 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP0707078A1 true EP0707078A1 (fr) | 1996-04-17 |
| EP0707078B1 EP0707078B1 (fr) | 2004-02-25 |
Family
ID=3756147
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP19940402832 Expired - Lifetime EP0707078B1 (fr) | 1994-09-26 | 1994-12-09 | Nouveau procédé de déplacement de jus de cane |
Country Status (5)
| Country | Link |
|---|---|
| EP (1) | EP0707078B1 (fr) |
| AU (1) | AU679255B2 (fr) |
| BR (1) | BR9404596A (fr) |
| DE (1) | DE69433575T2 (fr) |
| DK (1) | DK0707078T3 (fr) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0769561A1 (fr) * | 1995-10-24 | 1997-04-23 | Michele Marcelle Amelie Riviere | Procédé d'extraction de jus à partir de canne à sucre |
| CN1089809C (zh) * | 1996-12-30 | 2002-08-28 | 米歇尔·马塞勒·阿梅利·里维埃 | 萃取甘蔗汁液的方法及装置 |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BRPI0900946A8 (pt) * | 2009-04-17 | 2017-05-16 | Empral Desenvolvimento De Equipamentos Ltda | Difusor horizontal com sistema de deslocamento da cana-de-açúcar e outros produtos por meio de cabos e empurradores retráteis |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1143640A (fr) * | ||||
| GB1095787A (en) * | 1965-06-04 | 1967-12-20 | Braunschweigische Maschb Ansta | Apparatus and method for the continuous extraction of sugar from sugar cane |
| FR2050660A5 (en) * | 1969-06-20 | 1971-04-02 | Fives Lille Cail | Sugar extraction from sugar cane |
| FR2310409A2 (fr) * | 1975-05-09 | 1976-12-03 | Fives Cail Babcock | Procede et installation pour l'extraction par diffusion du sucre de la bagasse de canne a sucre |
| FR2477177A2 (fr) * | 1980-02-29 | 1981-09-04 | Fives Cail Babcock | Installation pour l'extraction par diffusion du sucre de la bagasse de canne a sucre |
| FR2507621A1 (fr) * | 1981-06-12 | 1982-12-17 | Rech Geolog Miniere | Procede d'extraction des matieres solubles des cannes a sucre et appareil de mise en oeuvre |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2278767A1 (fr) * | 1974-04-11 | 1976-02-13 | Fives Cail Babcock | Procede et installation pour l'extraction par diffusion du sucre de la bagasse de canne a sucre |
| MX166939B (es) * | 1989-04-21 | 1993-02-15 | Biotecnologia Y Derivados De M | Sistema mejorado de baja presion para la extraccion de solubles de materia fibrosa |
-
1994
- 1994-09-26 AU AU74195/94A patent/AU679255B2/en not_active Ceased
- 1994-11-21 BR BR9404596A patent/BR9404596A/pt not_active Application Discontinuation
- 1994-12-09 DK DK94402832T patent/DK0707078T3/da active
- 1994-12-09 EP EP19940402832 patent/EP0707078B1/fr not_active Expired - Lifetime
- 1994-12-09 DE DE1994633575 patent/DE69433575T2/de not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1143640A (fr) * | ||||
| GB1095787A (en) * | 1965-06-04 | 1967-12-20 | Braunschweigische Maschb Ansta | Apparatus and method for the continuous extraction of sugar from sugar cane |
| FR2050660A5 (en) * | 1969-06-20 | 1971-04-02 | Fives Lille Cail | Sugar extraction from sugar cane |
| FR2310409A2 (fr) * | 1975-05-09 | 1976-12-03 | Fives Cail Babcock | Procede et installation pour l'extraction par diffusion du sucre de la bagasse de canne a sucre |
| FR2477177A2 (fr) * | 1980-02-29 | 1981-09-04 | Fives Cail Babcock | Installation pour l'extraction par diffusion du sucre de la bagasse de canne a sucre |
| FR2507621A1 (fr) * | 1981-06-12 | 1982-12-17 | Rech Geolog Miniere | Procede d'extraction des matieres solubles des cannes a sucre et appareil de mise en oeuvre |
Non-Patent Citations (1)
| Title |
|---|
| G.P.MEADE ET AL.: "Cane Sugar Handbook", JOHN WILEY & SONS, NEW YORK ,N.Y. * |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0769561A1 (fr) * | 1995-10-24 | 1997-04-23 | Michele Marcelle Amelie Riviere | Procédé d'extraction de jus à partir de canne à sucre |
| US5772775A (en) * | 1995-10-24 | 1998-06-30 | Riviere; Michele Marcelle Amelie | Method of extraction of juice from sugar cane |
| CN1089809C (zh) * | 1996-12-30 | 2002-08-28 | 米歇尔·马塞勒·阿梅利·里维埃 | 萃取甘蔗汁液的方法及装置 |
Also Published As
| Publication number | Publication date |
|---|---|
| AU679255B2 (en) | 1997-06-26 |
| DE69433575D1 (de) | 2004-04-01 |
| DK0707078T3 (da) | 2004-06-28 |
| AU7419594A (en) | 1996-04-18 |
| DE69433575T2 (de) | 2005-03-31 |
| EP0707078B1 (fr) | 2004-02-25 |
| BR9404596A (pt) | 1995-08-01 |
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| Date | Code | Title | Description |
|---|---|---|---|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
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| 17P | Request for examination filed |
Effective date: 19961114 |
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| RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: RIVIERE, MICHELE MARCELLE AMELIE, NEE PAYET |
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| RIN1 | Information on inventor provided before grant (corrected) |
Inventor name: RIVIERE, MAXIME |
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