EP0899344A2 - Procédé et appareil pour production de jus à partir de bettraves sucrières - Google Patents
Procédé et appareil pour production de jus à partir de bettraves sucrières Download PDFInfo
- Publication number
- EP0899344A2 EP0899344A2 EP98113070A EP98113070A EP0899344A2 EP 0899344 A2 EP0899344 A2 EP 0899344A2 EP 98113070 A EP98113070 A EP 98113070A EP 98113070 A EP98113070 A EP 98113070A EP 0899344 A2 EP0899344 A2 EP 0899344A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- beet
- juice
- sugar
- solid
- separating
- 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
- 235000011389 fruit/vegetable juice Nutrition 0.000 title claims abstract description 45
- 238000000034 method Methods 0.000 title claims abstract description 30
- 240000000111 Saccharum officinarum Species 0.000 title 1
- 235000007201 Saccharum officinarum Nutrition 0.000 title 1
- 235000016068 Berberis vulgaris Nutrition 0.000 claims abstract description 34
- 241000335053 Beta vulgaris Species 0.000 claims abstract description 34
- 239000007787 solid Substances 0.000 claims abstract description 19
- 241000219310 Beta vulgaris subsp. vulgaris Species 0.000 claims abstract description 18
- 235000021536 Sugar beet Nutrition 0.000 claims abstract description 18
- 102000004169 proteins and genes Human genes 0.000 claims abstract description 18
- 108090000623 proteins and genes Proteins 0.000 claims abstract description 18
- 235000000346 sugar Nutrition 0.000 claims abstract description 18
- 239000007788 liquid Substances 0.000 claims abstract description 13
- 238000000227 grinding Methods 0.000 claims abstract description 7
- 241000196324 Embryophyta Species 0.000 claims abstract description 6
- 238000000926 separation method Methods 0.000 claims description 13
- 238000000605 extraction Methods 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 9
- 239000003792 electrolyte Substances 0.000 claims description 4
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 2
- 238000002156 mixing Methods 0.000 claims description 2
- 230000001376 precipitating effect Effects 0.000 claims description 2
- 238000003825 pressing Methods 0.000 claims description 2
- 230000006920 protein precipitation Effects 0.000 claims description 2
- 238000003801 milling Methods 0.000 claims 2
- 239000002253 acid Substances 0.000 claims 1
- 230000003068 static effect Effects 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 238000010297 mechanical methods and process Methods 0.000 abstract 1
- 230000005226 mechanical processes and functions Effects 0.000 abstract 1
- 238000001556 precipitation Methods 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 11
- 150000001413 amino acids Chemical class 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 4
- 241001465754 Metazoa Species 0.000 description 4
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 3
- 235000011941 Tilia x europaea Nutrition 0.000 description 3
- 239000004571 lime Substances 0.000 description 3
- 229920001277 pectin Polymers 0.000 description 3
- 239000001814 pectin Substances 0.000 description 3
- 235000010987 pectin Nutrition 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- 241000283690 Bos taurus Species 0.000 description 2
- 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 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 235000015191 beet juice Nutrition 0.000 description 2
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 2
- 239000000920 calcium hydroxide Substances 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 229930006000 Sucrose Natural products 0.000 description 1
- 239000006053 animal diet Substances 0.000 description 1
- 230000001914 calming effect Effects 0.000 description 1
- 239000008162 cooking oil Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229940082150 encore Drugs 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 235000015203 fruit juice Nutrition 0.000 description 1
- 235000021552 granulated sugar Nutrition 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000012263 liquid product Substances 0.000 description 1
- 230000002503 metabolic effect Effects 0.000 description 1
- 235000013379 molasses Nutrition 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000005720 sucrose Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B5/00—Reducing the size of material from which sugar is to be extracted
- C13B5/06—Slicing sugar beet
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B10/00—Production of sugar juices
- C13B10/08—Extraction of sugar from sugar beet with water
Definitions
- the invention relates to a method and an installation for the extraction of juice from sugar beet for the industrial Sugar production, in which the previously washed Sugar beets are crushed and the crushed Beet mass separated into a solid and a liquid phase becomes.
- Another problem is the protein present in the beet, which is broken down into amino acids in the process, in the heated extraction tower, which then make it necessary to control the pH by adding calcium hydroxide and to add the amino acids from the juice produced remove. This is because the amino acids change the pH value, are the cause of an inversion of the sucrose, thus lead to sugar losses and are a hindrance to sugar crystallization.
- the amino acids generated in the process are bound with lime and the protein, which can be used as animal feed, is lost for further useful use.
- the amino acids are spread with the lime on agricultural fields and have hardly any fertilizer value there, while the proteins contained in the beets are intrinsically valuable animal feed, which is lost in this process.
- a third problem is with the beets in the process introduced bacteria that the beets during their storage do nothing because they are during the beet campaign prevailing outside temperatures are idle, the but at the temperatures of juice making by the Heat in the extraction tower become very active and not only eat sugar, but through their metabolic products make the juice sour what you add by adding of formalin has to compensate. This offer is over questionable for various reasons.
- the invention avoids the disadvantages of the prior art Technology. It is the object of the invention with simple Means the process of juice production at continuous To design the procedure so that the Juice extraction from those who dominate the beet campaign Temperatures and therefore energetically essential runs cheaper and that the contained in the beet Protein can be fed to the animal diet can, and execute the process so that the with the Sugar beet bacteria introduced into the process cannot take effect.
- the invention is that the crushing of Sugar beet at normal outside temperature during the Beet campaign takes place through a grinding process in which the cells are mechanically disrupted, but not completely be torn apart that the ground Beet mass at the same temperature in a separation stage, e.g. a centrifuge or press, in their liquid Part and their fixed part separates that one then the fixed portion of a further grinding process subjects, in which the cells are further unlocked and then the ground product at the same temperature in another separation device, e.g. one High performance centrifuge, again in a liquid and separates a fixed part that the cold obtained Juice quickly heated to about 90 ° for a short time, him sterilized with it, and then in a small amount Precipitants, e.g. an electrolyte, admixed and in this way the protein in the juice fails, that is removed from the juice in a separation stage, and that the juice obtained is now for further processing feeds while you have the precipitated protein added to the separated solid part.
- a separation stage
- This process can be operated continuously uses considerably less energy because only the one received Juice, but not solid matter and in the extraction tower added water must be heated, the The use of lime is eliminated, the use of chemicals has decreased, in particular the use is no longer applicable of formalin and sulfur dioxide. It will Protein as such is separated and can in the course of the process can be used as cattle feed by adding up to the low sugar residues otherwise only contain fiber Solid mass is mixed.
- a system is used to carry out this method for the extraction of juice from sugar beet for sugar production with a beet washer, a beet shredder and a separator, which is characterized in that the beet crushing device a grinder or grater is through their grinding process, that at normal outside temperature during the beet campaign, the cells take place mechanically open minded, but not completely torn apart be that the beet grinder a separator, preferably a centrifuge or press, which is the crushed Beet mass in a liquid portion and a solid Part separates that a collection vessel for the liquid part or a pipeline is provided and that to the output of the separator for the fixed portion another shredder connected and this another separation device, preferably in the form of a centrifuge, downstream that a device for the short-term for the juice obtained High heating and a station for adding electrolyte and protein precipitation are downstream that this Station a separator for separating the precipitated Protein is downstream and that this facility a station to hand over the now pure juice downstream of
- the resulting pectin can also be obtained by separating it from the process.
- the drawing shows a block diagram of the system according to the invention: Washed sugar beets are fed via a conveyor belt 1 to a mill 2 or grater, the screw conveyor of which feeds the sugar beets to the grinder or grater. During this grinding process, the sugar beet cells are torn open and mechanically disrupted, but not completely destroyed.
- the crushed beet mass is fed by means of a conveyor 3 to a first separation stage in the form of the centrifuge 4, from which the liquid product portion of juice is fed to the heat exchanger 7 serving as a heating device, in which the beet juice is heated to a temperature of approximately 90 ° C is heated in a short time.
- the solid obtained in the first separation stage 4 is fed to a further mill 5 by means of a further conveyor and is ground in the latter in such a way that the cells are completely broken down.
- the liquid part of this mass obtained is also fed to the heating device 7 after it has been separated from the solids content in the separation stage 6.
- the heating device passes through a mixing device 8, in which the juice is supplied with a means for precipitating the protein by means of the feed pump 9.
- the juice then flows into a calming vessel 10, where the protein flocculates.
- the protein is separated in the downstream separator 11 and fed to the mixer 13 by means of the conveying device 12.
- the juice running out of the separator 11 is then fed to further processing into sugar products, such as granulated sugar, liquid sugar, rock candy, etc.
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Fodder In General (AREA)
- Non-Alcoholic Beverages (AREA)
- Fats And Perfumes (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19736080 | 1997-08-20 | ||
| DE19736080A DE19736080A1 (de) | 1997-08-20 | 1997-08-20 | Verfahren und Anlage zur Gewinnung von Saft aus Zuckerrüben |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| EP0899344A2 true EP0899344A2 (fr) | 1999-03-03 |
| EP0899344A3 EP0899344A3 (fr) | 2002-10-02 |
| EP0899344B1 EP0899344B1 (fr) | 2004-05-26 |
Family
ID=7839532
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP98113070A Expired - Lifetime EP0899344B1 (fr) | 1997-08-20 | 1998-07-14 | Procédé et appareil pour production de jus à partir de bettraves sucrières |
Country Status (2)
| Country | Link |
|---|---|
| EP (1) | EP0899344B1 (fr) |
| DE (2) | DE19736080A1 (fr) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007068378A1 (fr) * | 2005-12-14 | 2007-06-21 | Hochschule Neubrandenburg | Procede et dispositif d'obtention d'un jus contenu dans un corps, par exemple un jus de fruits, un jus de legumes ou similaires |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE10144486C1 (de) * | 2001-09-10 | 2003-04-24 | Karlsruhe Forschzent | Verfahren zum kontinuierlichen nichtthermischen Aufschluß und Pasteurisieren industrieller Mengen organischen Prozessguts durch Elektroporation und Reaktor zum Durchführen des Verfahrens |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3477873A (en) * | 1966-10-03 | 1969-11-11 | Beloit Corp | Sugar beet processing |
| DE3150314C2 (de) * | 1981-12-18 | 1986-03-27 | Fried. Krupp Gmbh, 4300 Essen | Verfahren zur Gewinnung einer Saccharose-Lösung aus Zuckerrüben und anderen saccharosehaltigen Pflanzen |
| DE3407364A1 (de) * | 1984-02-29 | 1985-08-29 | Pfeifer & Langen, 5000 Köln | Naturbelassener vollrohrzucker und verfahren zu seiner herstellung |
| AT401776B (de) * | 1989-03-10 | 1996-11-25 | Agrana Zucker Gmbh | Mehrstufiges verfahren zur zuckergewinnung aus zuckerrüben |
-
1997
- 1997-08-20 DE DE19736080A patent/DE19736080A1/de not_active Withdrawn
-
1998
- 1998-07-14 DE DE59811450T patent/DE59811450D1/de not_active Expired - Fee Related
- 1998-07-14 EP EP98113070A patent/EP0899344B1/fr not_active Expired - Lifetime
Non-Patent Citations (1)
| Title |
|---|
| None |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007068378A1 (fr) * | 2005-12-14 | 2007-06-21 | Hochschule Neubrandenburg | Procede et dispositif d'obtention d'un jus contenu dans un corps, par exemple un jus de fruits, un jus de legumes ou similaires |
Also Published As
| Publication number | Publication date |
|---|---|
| DE19736080A1 (de) | 1999-02-25 |
| DE59811450D1 (de) | 2004-07-01 |
| EP0899344B1 (fr) | 2004-05-26 |
| EP0899344A3 (fr) | 2002-10-02 |
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