EP0126512A1 - Verfahren zur Gewinnung von Disacchariden aus Disaccharide enthaltenden Tuberosen durch Extraktion mit nicht erwärmtem Wasser - Google Patents
Verfahren zur Gewinnung von Disacchariden aus Disaccharide enthaltenden Tuberosen durch Extraktion mit nicht erwärmtem Wasser Download PDFInfo
- Publication number
- EP0126512A1 EP0126512A1 EP84200723A EP84200723A EP0126512A1 EP 0126512 A1 EP0126512 A1 EP 0126512A1 EP 84200723 A EP84200723 A EP 84200723A EP 84200723 A EP84200723 A EP 84200723A EP 0126512 A1 EP0126512 A1 EP 0126512A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- sugar
- water
- disaccharides
- extraction
- beets
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 34
- 238000000034 method Methods 0.000 title claims abstract description 29
- 150000002016 disaccharides Chemical class 0.000 title claims abstract description 11
- 238000011084 recovery Methods 0.000 title claims abstract description 8
- 238000000605 extraction Methods 0.000 title claims description 19
- 235000000346 sugar Nutrition 0.000 claims abstract description 60
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 12
- 239000000463 material Substances 0.000 claims abstract description 10
- 238000005115 demineralization Methods 0.000 claims abstract description 3
- 239000007788 liquid Substances 0.000 claims description 4
- 238000005342 ion exchange Methods 0.000 claims 1
- 239000007858 starting material Substances 0.000 abstract description 6
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 30
- 241000335053 Beta vulgaris Species 0.000 description 25
- 235000016068 Berberis vulgaris Nutrition 0.000 description 21
- 241000219310 Beta vulgaris subsp. vulgaris Species 0.000 description 20
- 235000021536 Sugar beet Nutrition 0.000 description 20
- 239000000243 solution Substances 0.000 description 13
- 238000005520 cutting process Methods 0.000 description 10
- 239000000126 substance Substances 0.000 description 8
- 235000013379 molasses Nutrition 0.000 description 7
- 239000012466 permeate Substances 0.000 description 7
- 235000018102 proteins Nutrition 0.000 description 7
- 102000004169 proteins and genes Human genes 0.000 description 7
- 108090000623 proteins and genes Proteins 0.000 description 7
- 150000003839 salts Chemical class 0.000 description 7
- 241000196324 Embryophyta Species 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 6
- 239000001814 pectin Substances 0.000 description 6
- 235000010987 pectin Nutrition 0.000 description 6
- 229920001277 pectin Polymers 0.000 description 6
- 238000009792 diffusion process Methods 0.000 description 5
- 150000002500 ions Chemical class 0.000 description 5
- 239000012465 retentate Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 150000001450 anions Chemical class 0.000 description 4
- 239000006227 byproduct Substances 0.000 description 4
- 238000002425 crystallisation Methods 0.000 description 4
- 230000008025 crystallization Effects 0.000 description 4
- 238000004925 denaturation Methods 0.000 description 4
- 230000036425 denaturation Effects 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 3
- CZMRCDWAGMRECN-UHFFFAOYSA-N Rohrzucker Natural products OCC1OC(CO)(OC2OC(CO)C(O)C(O)C2O)C(O)C1O CZMRCDWAGMRECN-UHFFFAOYSA-N 0.000 description 3
- 235000011941 Tilia x europaea Nutrition 0.000 description 3
- 239000004571 lime Substances 0.000 description 3
- 239000012528 membrane Substances 0.000 description 3
- BITYAPCSNKJESK-UHFFFAOYSA-N potassiosodium Chemical class [Na].[K] BITYAPCSNKJESK-UHFFFAOYSA-N 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 235000021552 granulated sugar Nutrition 0.000 description 2
- 238000003306 harvesting Methods 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 229920001592 potato starch Polymers 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000012047 saturated solution Substances 0.000 description 2
- 235000020374 simple syrup Nutrition 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 241000894007 species Species 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- 102000009027 Albumins Human genes 0.000 description 1
- 108010088751 Albumins Proteins 0.000 description 1
- 235000021533 Beta vulgaris Nutrition 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 229920000298 Cellophane Polymers 0.000 description 1
- DSLZVSRJTYRBFB-LLEIAEIESA-N D-glucaric acid Chemical compound OC(=O)[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C(O)=O DSLZVSRJTYRBFB-LLEIAEIESA-N 0.000 description 1
- WHUUTDBJXJRKMK-UHFFFAOYSA-N Glutamic acid Natural products OC(=O)C(N)CCC(O)=O WHUUTDBJXJRKMK-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- ONIBWKKTOPOVIA-BYPYZUCNSA-N L-Proline Chemical compound OC(=O)[C@@H]1CCCN1 ONIBWKKTOPOVIA-BYPYZUCNSA-N 0.000 description 1
- WHUUTDBJXJRKMK-VKHMYHEASA-N L-glutamic acid Chemical compound OC(=O)[C@@H](N)CCC(O)=O WHUUTDBJXJRKMK-VKHMYHEASA-N 0.000 description 1
- COLNVLDHVKWLRT-QMMMGPOBSA-N L-phenylalanine Chemical compound OC(=O)[C@@H](N)CC1=CC=CC=C1 COLNVLDHVKWLRT-QMMMGPOBSA-N 0.000 description 1
- AYFVYJQAPQTCCC-GBXIJSLDSA-N L-threonine Chemical compound C[C@@H](O)[C@H](N)C(O)=O AYFVYJQAPQTCCC-GBXIJSLDSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 235000021534 Mangelwurzel Nutrition 0.000 description 1
- ONIBWKKTOPOVIA-UHFFFAOYSA-N Proline Natural products OC(=O)C1CCCN1 ONIBWKKTOPOVIA-UHFFFAOYSA-N 0.000 description 1
- 235000002595 Solanum tuberosum Nutrition 0.000 description 1
- 244000061456 Solanum tuberosum Species 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- 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 1
- AYFVYJQAPQTCCC-UHFFFAOYSA-N Threonine Natural products CC(O)C(N)C(O)=O AYFVYJQAPQTCCC-UHFFFAOYSA-N 0.000 description 1
- 239000004473 Threonine Substances 0.000 description 1
- 150000007513 acids Chemical group 0.000 description 1
- 239000003957 anion exchange resin Substances 0.000 description 1
- 235000015191 beet juice Nutrition 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 235000011116 calcium hydroxide Nutrition 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- UGZVNIRNPPEDHM-SBBOJQDXSA-L calcium;(2s,3s,4s,5r)-2,3,4,5-tetrahydroxyhexanedioate Chemical compound [Ca+2].[O-]C(=O)[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C([O-])=O UGZVNIRNPPEDHM-SBBOJQDXSA-L 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 239000003729 cation exchange resin Substances 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 230000001427 coherent effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000002242 deionisation method Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000011026 diafiltration Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 235000013922 glutamic acid Nutrition 0.000 description 1
- 239000004220 glutamic acid Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000002706 hydrostatic effect Effects 0.000 description 1
- 229960004903 invert sugar Drugs 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000035772 mutation Effects 0.000 description 1
- 235000008935 nutritious Nutrition 0.000 description 1
- 230000003204 osmotic effect Effects 0.000 description 1
- COLNVLDHVKWLRT-UHFFFAOYSA-N phenylalanine Natural products OC(=O)C(N)CC1=CC=CC=C1 COLNVLDHVKWLRT-UHFFFAOYSA-N 0.000 description 1
- 235000008729 phenylalanine Nutrition 0.000 description 1
- 229960005190 phenylalanine Drugs 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229910001414 potassium ion Inorganic materials 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 235000013930 proline Nutrition 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000011403 purification operation Methods 0.000 description 1
- 238000009738 saturating Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 235000008521 threonine Nutrition 0.000 description 1
Classifications
-
- 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
- C13B10/10—Continuous processes
-
- 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
- C13B20/165—Purification of sugar juices by physical means, e.g. osmosis or filtration using membranes, e.g. osmosis, ultrafiltration
Definitions
- the invention relates to a process for the recovery of disaccharides from disaccharides containing tuberous plants according to which a solution of disaccharides in water is first subjected to ultrafiltration and subsequently to deionization.
- the so-obtained sterile thin juice can be completely freed of all salts by means of cation- and anion exchangers so that a solution is obtained which completely corresponds with the refined juice.
- a sugar is recovered which does not contain molasses as a by-product which generally contains at least 1/6 of the sugar from the beets and is inferior in comparison with sugar.
- colloidal products which have been removed separately contain proteins, glutamic acid, threonine, proline and phenyl alanine which are more valuable than molasses.
- the water used for the extraction should be as pure as possible.
- the water should not contain soluble substances which affect the purification of the juice.
- Especially water containing alkaline metal salts is disadvantageous because such salts inhibit the crystallization of large amounts of sugar and increase thereby the not contemplated molasses yield.
- the crude juice is heated at 85°C and mixed with an excess of slaked lime.
- the present free acids form therewith insoluble salts which with many other contaminations for instance proteins flocculate.
- a part of the lime forms calcium monosaccharate and another part dissolves.
- the slimy precipitate cannot be filtrated. For that reason carbon dioxide gas and steam are introduced so that the saccharate is decomposed and forms with the dissolved lime insoluble calcium carbonate which can be filtrated.
- the sugar present therein does not need to be extracted by diffusion as necessary with cuttings but sugar present in dissolved form in the cells of the tuberous plants can be rinsed out by simply washing with water of less than 60°C of the cells crushed by the mechanical treatment.
- the mechanical production of a mush may for instance be carried out by grating with a in the potato industry usual grating apparatus, a centrifugal pump with open blower or an oscillating mill, however, preferably with the mentioned grating apparatus.
- the permeate contains more sodium- and potassium salts than thin juice which is obtained according to the classic method because a considerable part of the potassium- and sodium salts which end up in the molasses according to the classic process now comes in the permeate according to the process according to the invention.
- the permeate should be led over an ion exchanger.
- the reduced mass is first separated for the most part from the liquid present therein and then subjected to an extraction with water of at most 10°C.
- the contact time at the extraction is at least 1 ⁇ 2 hour but such contact time is seldom necessary because in fact the extraction is momentary at the first contact with water.
- the amount of water used for the extraction is chosen in such a way that the obtained sugar solution has a sugar content of 12-14 % by weight.
- a further important advantage of the present process is that the ultrafiltrated ion-exchanged and concentrated permeate is so pure that for obtaining of almost pure beet sugar the crystallization does not need to be carried out in many stages and finally molasses is obtained as by-product. It is self-evident that the concentrated solution can be concentrated and/or cooled to saturation so that the sugar present therein crystallizes out but this operation is not necessary for the purification. Delivery of pure concentrated sugar syrup is also important for economic reasons because there are many technical uses for sugar which start with a concentrated solution.
- Another advantage is that according to the present process no sugar-foreign substances should be added to effect specific reactions which substances should be removed again after the end of the reaction.
- the present process is namely carried out without the addition of any reaction component.
- decennia beet sugar is recovered from sugar beets with a sugar content of 16-19 % by weigth by extracting the sugar beets with water in the above described way, followed by roughly removing the pulp, treating the obtained product with lime and carbon dioxide for precipitating the pectins and albumins followed by removing the precipitate concentrating the obtained juice (thin juice) by evaporation, crystallizing sugar from the saturated solution and separating the crystallized sugar.
- Mangels or mangolds give the highest yield of beets per surface unit and also the highest yield of sugar per surface unit but the sugar content per beet is low so that much pulp will be obtained as by-product. Usually they are ripe very late so they have much foliage at the harvest time.
- beet species utilizes the water supply of the soil much better than other beet species. For that reason they are better resistent against long periods of dryness. With the same amount of water respectively nutritious substances they produce more dry material than sugar beets. However, for the recovery of sugar according to the known process they are not suitable because the amount of pulp which is obtained per weight unit of beets is considerably larger than when sugar beets are used as starting material and moreover the sugar content per weight unit of beets is much lower.
- Sugar beets posess a high sugar content but give less beets per surface unit than whis.
- the amount of foliage thereof is at the harvest time much less than that of the original Beta-vulgaris and the axes because they are ripe early.
- the first stage was fed with mush from the grater which was mixed with diluted cell juice from the second stage.
- the retentate contained proteins, pectins and gums which for instance were mixed with the obtained desugarized pulp and sold as cattle-fodder.
- the permeate was further purified by leading it over ion exchangers and treating it with decolorizing absorbentia.
- the mush from the grating apparatus of example I was desugarized and dewatered by means of a multi-stage counter-current washing in centrifugal sieves.
- the somewhat diluted cell juice was subjected to a combination of ultrafiltration. Before the diafiltration 90 kg of water of 9°C were added to dilute the 89 kg of retentate of the first ultrafiltration and to desugarize it for the most part.
- the final retentate contained only 1% by weight of sugar.
- the so purified permeate or filtrate with a mass of 900 kg contained 9.7 % by weight of sugar (polarimetric) and 13.4 (w/w) % of dry material.
- the content of invert sugar was 5.4 (w/w) % on the basis of the dry material.
- This purified juice was then demineralized by means of subsequently a cation exchange resin and an anion exchange resin.
- This purified juice was almost colourless and contained only 5 (w/w) % non-sugar substances on the basis of the dry material content.
- This juice was concentrated in an evaporator to 71 (w/w) % dry material content.
- the white sugar obtained by crystallization was of excellent quality and was not second to other granulated sugar.
- This mush was then treated in the same way as described in example III.
- the pulp in the last stage was desugarized with 235 kg water of 3°C.
- the centrifugate of this fourth stage was used to desugarize the centrifugated pulp from the second stage. This was done in the third stage.
- the centrifugate was led to the centrifugated pulp from the first stage and the pulp from the third stage was led to the fourth stage.
- the mixture of centrifugates, coming from the third stage and pulp of the first stage were dewatered in the second stage.
- the juice from the second stage was joined with undiluted cell juice from the first stage. In this way a somewhat diluted cell juice (520 kg) was obtained, which was led to the ultrafiltration for the first purification with respect to proteins, gums and pectins.
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Coloring Foods And Improving Nutritive Qualities (AREA)
- Saccharide Compounds (AREA)
- Medicines Containing Plant Substances (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Compounds Of Unknown Constitution (AREA)
- Inorganic Insulating Materials (AREA)
- Non-Silver Salt Photosensitive Materials And Non-Silver Salt Photography (AREA)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT84200723T ATE21527T1 (de) | 1983-05-19 | 1984-05-17 | Verfahren zur gewinnung von disacchariden aus disaccharide enthaltenden tuberosen durch extraktion mit nicht erwaermtem wasser. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL8301786 | 1983-05-19 | ||
NL8301786A NL8301786A (nl) | 1983-05-19 | 1983-05-19 | Werkwijze voor het winnen van disacchariden uit disacchariden bevattende knolgewassen, onder toepassing van een extractie met onverwarmd water. |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0126512A1 true EP0126512A1 (de) | 1984-11-28 |
EP0126512B1 EP0126512B1 (de) | 1986-08-20 |
Family
ID=19841883
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP84200723A Expired EP0126512B1 (de) | 1983-05-19 | 1984-05-17 | Verfahren zur Gewinnung von Disacchariden aus Disaccharide enthaltenden Tuberosen durch Extraktion mit nicht erwärmtem Wasser |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP0126512B1 (de) |
JP (1) | JPS59224699A (de) |
AT (1) | ATE21527T1 (de) |
CS (1) | CS254326B2 (de) |
DE (1) | DE3460505D1 (de) |
NL (1) | NL8301786A (de) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1992008810A1 (en) * | 1990-11-09 | 1992-05-29 | Applied Membrane Systems Pty. Ltd. | A method and apparatus for fractionation of sugar containing solution |
WO2000060128A1 (en) * | 1999-04-07 | 2000-10-12 | Aeci Limited | Treatment of sugar juice |
WO2001014594A2 (en) * | 1999-08-19 | 2001-03-01 | Tate & Lyle, Inc. | Sugar beet membrane filtration process |
WO2001014595A2 (en) * | 1999-08-19 | 2001-03-01 | Tate & Lyle, Inc. | Sugar cane membrane filtration process |
US6375751B2 (en) | 1999-08-19 | 2002-04-23 | Tate & Lyle, Inc. | Process for production of purified cane juice for sugar manufacture |
US6387186B1 (en) | 1999-08-19 | 2002-05-14 | Tate & Lyle, Inc. | Process for production of purified beet juice for sugar manufacture |
US6406547B1 (en) | 2000-07-18 | 2002-06-18 | Tate & Lyle Industries, Limited | Sugar beet membrane filtration process |
US6440222B1 (en) | 2000-07-18 | 2002-08-27 | Tate & Lyle Industries, Limited | Sugar beet membrane filtration process |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102008020429B4 (de) * | 2008-04-24 | 2012-02-02 | Südzucker AG Mannheim/Ochsenfurt | Verfahren zur Elektroporation von Rübenschnitzeln und Vorrichtung zur Durchführung dieses Verfahrens |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL79743C (de) * | ||||
US2382407A (en) * | 1942-02-12 | 1945-08-14 | Barron Gray Packing Company | Extraction process |
GB1361674A (en) * | 1971-04-23 | 1974-07-30 | Danske Sukkerfab | Process for the purification and clarification of sugar juices |
-
1983
- 1983-05-19 NL NL8301786A patent/NL8301786A/nl not_active Application Discontinuation
-
1984
- 1984-05-17 AT AT84200723T patent/ATE21527T1/de not_active IP Right Cessation
- 1984-05-17 DE DE8484200723T patent/DE3460505D1/de not_active Expired
- 1984-05-17 EP EP84200723A patent/EP0126512B1/de not_active Expired
- 1984-05-18 JP JP59098872A patent/JPS59224699A/ja active Granted
- 1984-05-18 CS CS843700A patent/CS254326B2/cs unknown
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL79743C (de) * | ||||
US2382407A (en) * | 1942-02-12 | 1945-08-14 | Barron Gray Packing Company | Extraction process |
GB1361674A (en) * | 1971-04-23 | 1974-07-30 | Danske Sukkerfab | Process for the purification and clarification of sugar juices |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1992008810A1 (en) * | 1990-11-09 | 1992-05-29 | Applied Membrane Systems Pty. Ltd. | A method and apparatus for fractionation of sugar containing solution |
US5454952A (en) * | 1990-11-09 | 1995-10-03 | Applied Membrand Systems Pty Ltd. | Method and apparatus for fractionation of sugar containing solution |
WO2000060128A1 (en) * | 1999-04-07 | 2000-10-12 | Aeci Limited | Treatment of sugar juice |
AU781362B2 (en) * | 1999-04-07 | 2005-05-19 | Ufion (Proprietary) Limited | Treatment of sugar juice |
US6709527B1 (en) | 1999-04-07 | 2004-03-23 | Ufion (Pty) Limited | Treatment of sugar juice |
WO2001014595A3 (en) * | 1999-08-19 | 2001-12-06 | Tate & Lyle Inc | Sugar cane membrane filtration process |
WO2001014594A3 (en) * | 1999-08-19 | 2001-12-06 | Tate & Lyle Inc | Sugar beet membrane filtration process |
US6375751B2 (en) | 1999-08-19 | 2002-04-23 | Tate & Lyle, Inc. | Process for production of purified cane juice for sugar manufacture |
US6387186B1 (en) | 1999-08-19 | 2002-05-14 | Tate & Lyle, Inc. | Process for production of purified beet juice for sugar manufacture |
WO2001014595A2 (en) * | 1999-08-19 | 2001-03-01 | Tate & Lyle, Inc. | Sugar cane membrane filtration process |
WO2001014594A2 (en) * | 1999-08-19 | 2001-03-01 | Tate & Lyle, Inc. | Sugar beet membrane filtration process |
US6406547B1 (en) | 2000-07-18 | 2002-06-18 | Tate & Lyle Industries, Limited | Sugar beet membrane filtration process |
US6440222B1 (en) | 2000-07-18 | 2002-08-27 | Tate & Lyle Industries, Limited | Sugar beet membrane filtration process |
Also Published As
Publication number | Publication date |
---|---|
CS370084A2 (en) | 1987-06-11 |
JPS59224699A (ja) | 1984-12-17 |
EP0126512B1 (de) | 1986-08-20 |
DE3460505D1 (en) | 1986-09-25 |
JPS6146119B2 (de) | 1986-10-13 |
ATE21527T1 (de) | 1986-09-15 |
CS254326B2 (en) | 1988-01-15 |
NL8301786A (nl) | 1984-12-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6663780B2 (en) | Method for the fractionation of molasses | |
RU2184148C2 (ru) | Способ для извлечения органического соединения из растворов | |
US5454952A (en) | Method and apparatus for fractionation of sugar containing solution | |
EP0820527B1 (de) | Verfahren zur rückgewinnung von xylose aus lösungen | |
US3734773A (en) | Process for selectively purifying sugar beet diffusion juice and by-product recovery of valuable organic acids therefrom | |
AU2004245136A1 (en) | Process for the production of crystalline xylose from sugar cane bagasse, crystalline xylose obtained by said process, process for the production of xylitol from the said xylose and crystalline xylitol obtained thereby | |
EP0126512B1 (de) | Verfahren zur Gewinnung von Disacchariden aus Disaccharide enthaltenden Tuberosen durch Extraktion mit nicht erwärmtem Wasser | |
US5624500A (en) | Syrup of natural carob sugars and a process for its production | |
SK3772002A3 (en) | Sugar beet membrane filtration process | |
EA015362B1 (ru) | Способ производства жидкого сахара | |
US4328043A (en) | Method of increasing sugar extraction efficiency from sugar-containing plant tissue with use of carbon dioxide | |
EP0126513B1 (de) | Verfahren zur Gewinnung von Monosacchariden aus Pflanzen welche Poly-, Oligo-, und/oder Disacchariden enthalten mittels Ultrafiltration | |
US5928429A (en) | Process for the enhancement of recovery of sugar | |
US4138272A (en) | Process for the obtention of fructose and fructose-rich syrups from xerophyte plants | |
EP0904251A1 (de) | Verfahren zur herstellung von hochreinen kaliumsalzen | |
JP4513075B2 (ja) | 炭酸ソーダの添加による軟化処理を含む限外ろ過処理による甘蔗からの精製糖製造プロセス | |
US20090145426A1 (en) | Refined sugar manufacturing process | |
US20120060832A1 (en) | Process for producing granulated refined sugar from sugar cane juice | |
Godshall | Sugar and other sweeteners | |
WO2006125286A1 (en) | Process for the production of pyrogen-free anhydrous crystalline dextrose of high purity from sucrose | |
PL140546B1 (en) | Method of obtaining,by water extraction,disaccharides from bulbiferous plants containing them | |
AU624560B1 (en) | Sugar refining process | |
US2150197A (en) | Manufacture of dextrose | |
US1044004A (en) | Process for recovery of cane-sugar. | |
US3745016A (en) | Process for purifying sugar beet diffusion juice |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AK | Designated contracting states |
Designated state(s): AT BE CH DE FR GB IT LI LU NL SE |
|
17P | Request for examination filed |
Effective date: 19841219 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE CH DE FR GB IT LI LU NL SE |
|
REF | Corresponds to: |
Ref document number: 21527 Country of ref document: AT Date of ref document: 19860915 Kind code of ref document: T |
|
ITF | It: translation for a ep patent filed |
Owner name: JACOBACCI & PERANI S.P.A. |
|
REF | Corresponds to: |
Ref document number: 3460505 Country of ref document: DE Date of ref document: 19860925 |
|
ET | Fr: translation filed | ||
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 19910507 Year of fee payment: 8 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: AT Payment date: 19910510 Year of fee payment: 8 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: SE Payment date: 19910521 Year of fee payment: 8 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 19910522 Year of fee payment: 8 |
|
ITTA | It: last paid annual fee | ||
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 19910531 Year of fee payment: 8 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: CH Payment date: 19910606 Year of fee payment: 8 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: LU Payment date: 19910607 Year of fee payment: 8 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 19910628 Year of fee payment: 8 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 19910705 Year of fee payment: 8 |
|
EPTA | Lu: last paid annual fee | ||
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19920517 Ref country code: GB Effective date: 19920517 Ref country code: AT Effective date: 19920517 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Effective date: 19920518 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Effective date: 19920531 Ref country code: CH Effective date: 19920531 Ref country code: BE Effective date: 19920531 |
|
BERE | Be: lapsed |
Owner name: COOPERATIEVE VERENIGING SUIKER UNIE U.A. Effective date: 19920531 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Effective date: 19921201 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 19920517 |
|
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee | ||
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Effective date: 19930129 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Effective date: 19930202 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST |
|
EUG | Se: european patent has lapsed |
Ref document number: 84200723.9 Effective date: 19921204 |