DE4778A - New elution process for obtaining sugar from molasses or syrup - Google Patents
New elution process for obtaining sugar from molasses or syrupInfo
- Publication number
- DE4778A DE4778A DE4778A DE 4778 A DE4778 A DE 4778A DE 4778 A DE4778 A DE 4778A
- Authority
- DE
- Germany
- Prior art keywords
- sugar
- lime
- molasses
- alcohol
- elution
- 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.)
- Pending
Links
- 235000000346 sugar Nutrition 0.000 title claims description 31
- 235000013379 molasses Nutrition 0.000 title claims description 20
- 238000000034 method Methods 0.000 title claims description 15
- 238000010828 elution Methods 0.000 title claims description 14
- 235000020357 syrup Nutrition 0.000 title description 2
- 239000006188 syrup Substances 0.000 title description 2
- 239000004571 lime Substances 0.000 claims description 25
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 23
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 23
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 12
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 7
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 5
- 238000002386 leaching Methods 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 4
- 150000008163 sugars Chemical class 0.000 claims description 4
- 235000015191 beet juice Nutrition 0.000 claims description 3
- 230000015572 biosynthetic process Effects 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 2
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 2
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims 2
- 239000003337 fertilizer Substances 0.000 claims 2
- 238000002156 mixing Methods 0.000 claims 2
- 238000005406 washing Methods 0.000 claims 2
- 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 claims 1
- 238000010521 absorption reaction Methods 0.000 claims 1
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 claims 1
- 229910052601 baryte Inorganic materials 0.000 claims 1
- 239000010428 baryte Substances 0.000 claims 1
- 238000007664 blowing Methods 0.000 claims 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims 1
- 235000011116 calcium hydroxide Nutrition 0.000 claims 1
- 239000000920 calcium hydroxide Substances 0.000 claims 1
- 239000003518 caustics Substances 0.000 claims 1
- 230000029142 excretion Effects 0.000 claims 1
- 238000000605 extraction Methods 0.000 claims 1
- 230000004720 fertilization Effects 0.000 claims 1
- 239000000706 filtrate Substances 0.000 claims 1
- 238000001914 filtration Methods 0.000 claims 1
- 239000001760 fusel oil Substances 0.000 claims 1
- 235000013336 milk Nutrition 0.000 claims 1
- 239000008267 milk Substances 0.000 claims 1
- 210000004080 milk Anatomy 0.000 claims 1
- 239000012452 mother liquor Substances 0.000 claims 1
- 238000001556 precipitation Methods 0.000 claims 1
- 229920006395 saturated elastomer Polymers 0.000 claims 1
- 239000002904 solvent Substances 0.000 claims 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- 235000012255 calcium oxide Nutrition 0.000 description 4
- 239000000292 calcium oxide Substances 0.000 description 4
- 230000007812 deficiency Effects 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 230000001476 alcoholic effect Effects 0.000 description 2
- 150000001408 amides Chemical class 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 159000000007 calcium salts Chemical class 0.000 description 2
- 238000003776 cleavage reaction Methods 0.000 description 2
- 230000007017 scission Effects 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- 125000003158 alcohol group Chemical group 0.000 description 1
- 150000001447 alkali salts Chemical class 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 206010016256 fatigue Diseases 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000012047 saturated solution Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Description
1878.1878.
Klasse 89.Class 89.
AUGUST DREVERMANN in DÜSSELDORF. Neues Elutionsverfahren zur Zuckergewinnung aus Melasse oder Syrup. AUGUST DREVERMANN in DÜSSELDORF. New elution process for obtaining sugar from molasses or syrup.
Patentirt im Deutschen Reiche vom 2. Februar 1878 ab.Patented in the German Empire on February 2, 1878.
Das bekannte Elutionsverfahren Scheibler's besitzt in dem Theile, der sich mit der Herstellung seines Ausgarigsmaterials, des Melassenrohkalkes, beschäftigt, sehr erhebliche Mängel, die sich besonders zeigen, wenn der Melassenrohkalk nach dem Verfahren des Dr. Seyferth dargestellt wird. Diese Mängel bestehen darin, dafs eine Anzahl der in der Melasse neben dem Zucker sich findenden organischen Nichtzuckerstoffe durch die hohe Temperatur beim Trocknen des Rohkalks oder durch die Heftigkeit der Reaction bei Einwirkung des Aetzkalkes (nach der Seyferth'sehen Methode seiner Darstellung), welche letztere die Temperatur bis zu 1250 C, und unter Umständen darüber, steigert, in ihrer chemischen Natur eine totale. Umänderung bezw. Spaltung erleiden. Es sind dies, wie ermittelt worden ist, namentlich stickstoffhaltige amidartige Körper, die sich bei dieser Art der Einwirkung des Kalkes in Ammoniak, Trimethylamin etc. einerseits und stickstofffreie bezw. stickstoffärmere Säuren andererseits spalten, welche dann als neugebildete Kalksalze in der Rohmasse zurückbleiben, während die Ammoniakbasen sich theilweise verflüchtigen. Diese neugebildeten Kalksalze bleiben wegen ihrer grofsen Schwerlöslichkeit bei nachherigem Auslaugen mit verdünntem Spiritus alsdann in dem ausgelaugten Zuckerkalk zurück. Wird letzterer nun demnächst zum Scheiden von Rübensaft benutzt, so treten diese Kalksalze als solche oder umgewandelt zu Alkalisalzen mit in den Scheidesaft über, um alle Stadien der Verarbeitung desselben zu durchlaufen und sich zuletzt in der resultirenden Melasse, namentlich bei Wiederholung der Operation, immer mehr anzusammeln. Eine solchergestalt gewonnene Melasse enthält nun nicht allein die ihr schon eigenthümlichen Amide, sondern auch die Spaltungssäuren solcher Amide der Melasse aus früheren Verarbeitungen, und es ist klar, dafs .sich im Laufe wiederholter Operationen diese Spaltungssäuren in dem erzielten, ausgewaschenen Zuckerkalk derart anhäufen, dafs von einer vorteilhaften Verwendung desselben zum Scheiden des Rübensaftes dann nicht mehr die Rede sein kann.Scheibler's well-known elution process has very considerable deficiencies in the part that deals with the production of its fermentation material, the raw molasses lime, which is particularly evident when the raw molasses lime is prepared according to the method of Dr. Seyferth is depicted. These deficiencies consist in the fact that a number of the organic non-sugar substances found in molasses as well as sugar are due to the high temperature during drying of the raw lime or due to the violence of the reaction under the action of the quicklime (according to Seyferth's method of its preparation), which latter the temperature up to 125 0 C, and under certain circumstances above, increases, in its chemical nature, a total. Change resp. Suffering from division. These are, as has been determined, namely nitrogen-containing amide-like bodies which, with this type of action of the lime in ammonia, trimethylamine, etc., on the one hand and nitrogen-free and respectively. On the other hand, low-nitrogen acids split, which then remain in the raw mass as newly formed calcium salts, while the ammonia bases are partly volatilized. These newly formed lime salts, because of their great poor solubility, then remain in the leached sugar lime when they are subsequently leached with dilute alcohol. If the latter is soon to be used for separating beet juice, these calcium salts, either as such or converted to alkali salts, also pass into the separating juice in order to pass through all stages of the processing of the same and finally become more and more in the resulting molasses, especially when the operation is repeated to accumulate. Molasses obtained in this way contains not only the amides peculiar to it, but also the cleavage acids of such amides of the molasses from earlier processing, and it is clear that in the course of repeated operations these cleavage acids accumulate in the washed-out sugar lime that is obtained of an advantageous use of the same for separating the beet juice can then no longer be spoken of.
Diese Mängel zu beseitigen bezw. das Elutionsverfahren so durchzuführen, dafs die organischen Nichtzuckerstoffe als solche in ihrer chemischen Natur unverändert erhalten bleiben, war Endzweck einer Reihe von Versuchen, die zu einem neuen Elutionsverfahren geführt haben, das gegenüber den bisherigen den Vorzug der rascheren, bequemeren Durchführbarkeit besitzt, einen reineren Zuckerkalk beim Auslaugen ergiebt, in Bezug auf Apparate eine wesentlich billigere Anlage gestattet, sowie weniger maschinelle und manuelle Arbeit erfordert.To eliminate these deficiencies respectively. to carry out the elution process in such a way that the organic Non-sugar substances as such remain unchanged in their chemical nature, was the end purpose of a series of attempts that led to a new elution process, which has the advantage over the previous ones that it can be carried out more quickly and conveniently, yields a purer sugar lime on leaching, and in relation to apparatus an essential one cheaper system permits and requires less mechanical and manual labor.
Das wesentliche des neuen Elutionsverfahrens besteht nun darin, dafs der Melasserohkalk nicht erst, wie bei dem älteren Scheiblerschen oder dem modificirten sogen. Scheibler-Seyferth'schen Verfahren auf dem zeitraubenden und kostspieligen Umweg als trockene, poröse Masse bei höherer Temperatur für sich hergestellt zu werden braucht, sondern im feinkörnigen Zustand innerhalb einer alkoholischen, gesättigten Lösung abfiltrirt und ausgewaschen wird. Es wird zu diesem Behufe bei der neuen Elution in der Weise verfahren, 'dafs eine Auflösung von Melasse in verdünntem Spiritus (von ca. 36 Volum-Procenten) einem Gemisch von feingepulvertem, frisch gebranntem, also wasserfreiem Aetzkalk, der mit einer solchen Menge stärkeren Alkohols durchtränkt ist, dafs er mit dem der Melasse eigenthümlichen Wassergehalt ebenfalls ca. 36 procentigen Spiritus bildet, in einem mit Rührwerk versehenen, geschlossenen Apparat zusammengebracht und die Mischung so lange im Umrühren erhalten wird, bis die suspendirten Kalkpartikelchen allen Zucker der alkoholischen Flüssigkeit aufgesogen und absorbirt haben, was sich in kurzer Zeit unter sehr mäfsiger Erwärmung allmälig vollzieht. Die Menge des angewendeten Aetzkalkes wird so bemessen, dafs dreibasischer Zuckerkalk entsteht und aufserdem noch genügend Kalk für die Freimachung der Alkalien der Nichtzuckerverbindungen vorhanden ist. Die vorherige Durchtränkung des Aetzkalkpulvers mit Alkohol ist zweckmäfsig, damit die Mischung mit der spirituosen Melasselösung ohne Schwierigkeit und namentlich ohne Klumpenbildung verläuft.The essential part of the new elution process consists in the fact that the molasses crude lime not just as with the older Scheibler or the modified so-called. Scheibler-Seyferth'schen Process on the time-consuming and costly detour as a dry, porous mass at a higher temperature in itself needs to be produced, but in the fine-grained state within an alcoholic, saturated solution is filtered off and washed out. It is for this purpose in the proceed with the new elution in such a way as to dissolve molasses in dilute Spirit (of approx. 36 percent by volume) a mixture of finely powdered, freshly burned, i.e. anhydrous quicklime, which is soaked with such an amount of stronger alcohol, that with the water content peculiar to molasses it is also about 36 percent alcohol forms, brought together in a closed apparatus equipped with a stirrer and the mixture is kept stirring until the particles of lime are suspended have soaked up and absorbed all the sugars in the alcoholic liquid that are in for a short time gradually with very moderate warming carries out. The amount of caustic lime applied is measured in such a way that it is three-basic Sugar lime is created and there is also enough lime to clear the alkalis of non-sugar compounds is present. The previous impregnation of the quicklime powder with alcohol is expedient so that the mixture with the liquor molasses solution proceeds without difficulty and especially without lump formation.
Nachdem die völlige Bindung des in der Lösung vorhandenen Zuckers durch den Aetzkalk sich unter sehr mäfsiger Wärmeentwicklung vollzogen hat, wird das Umrühren der MischungAfter the complete binding of the sugar present in the solution by the quicklime has taken place with very moderate heat development, the mixture is stirred
Claims (6)
Family
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