MXPA96001323A - Product to stabilize the sucrose contained in the sugar cane and application method - Google Patents
Product to stabilize the sucrose contained in the sugar cane and application methodInfo
- Publication number
- MXPA96001323A MXPA96001323A MXPA/A/1996/001323A MX9601323A MXPA96001323A MX PA96001323 A MXPA96001323 A MX PA96001323A MX 9601323 A MX9601323 A MX 9601323A MX PA96001323 A MXPA96001323 A MX PA96001323A
- Authority
- MX
- Mexico
- Prior art keywords
- product
- application
- sucrose
- sugar cane
- sucrose contained
- Prior art date
Links
- 229930006000 Sucrose Natural products 0.000 title claims abstract description 58
- 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 title claims abstract description 58
- 239000005720 sucrose Substances 0.000 title claims abstract description 58
- 240000000111 Saccharum officinarum Species 0.000 title claims abstract description 39
- 235000007201 Saccharum officinarum Nutrition 0.000 title claims abstract description 39
- 238000000034 method Methods 0.000 title claims abstract description 33
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 11
- 230000000087 stabilizing effect Effects 0.000 claims abstract description 11
- 230000000844 anti-bacterial effect Effects 0.000 claims abstract description 7
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims abstract description 6
- 150000003839 salts Chemical class 0.000 claims abstract description 6
- 150000003505 terpenes Chemical class 0.000 claims abstract description 6
- 235000007586 terpenes Nutrition 0.000 claims abstract description 6
- 239000007853 buffer solution Substances 0.000 claims abstract description 5
- 230000002255 enzymatic effect Effects 0.000 claims abstract description 4
- 239000003599 detergent Substances 0.000 claims abstract description 3
- 238000011012 sanitization Methods 0.000 claims abstract description 3
- 239000004094 surface-active agent Substances 0.000 claims abstract description 3
- 239000013543 active substance Substances 0.000 claims abstract 4
- 239000007864 aqueous solution Substances 0.000 claims abstract 2
- 235000011389 fruit/vegetable juice Nutrition 0.000 claims description 44
- 235000000346 sugar Nutrition 0.000 claims description 39
- 239000000463 material Substances 0.000 claims description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 6
- ZTQSAGDEMFDKMZ-UHFFFAOYSA-N butyric aldehyde Natural products CCCC=O ZTQSAGDEMFDKMZ-UHFFFAOYSA-N 0.000 claims description 6
- -1 ammonium ions Chemical class 0.000 claims description 5
- KBPLFHHGFOOTCA-UHFFFAOYSA-N 1-Octanol Chemical compound CCCCCCCCO KBPLFHHGFOOTCA-UHFFFAOYSA-N 0.000 claims description 4
- BBMCTIGTTCKYKF-UHFFFAOYSA-N 1-heptanol Chemical compound CCCCCCCO BBMCTIGTTCKYKF-UHFFFAOYSA-N 0.000 claims description 4
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims description 4
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims description 4
- NBBJYMSMWIIQGU-UHFFFAOYSA-N Propionic aldehyde Chemical compound CCC=O NBBJYMSMWIIQGU-UHFFFAOYSA-N 0.000 claims description 4
- HUMNYLRZRPPJDN-UHFFFAOYSA-N benzaldehyde Chemical compound O=CC1=CC=CC=C1 HUMNYLRZRPPJDN-UHFFFAOYSA-N 0.000 claims description 4
- ZSIAUFGUXNUGDI-UHFFFAOYSA-N hexan-1-ol Chemical compound CCCCCCO ZSIAUFGUXNUGDI-UHFFFAOYSA-N 0.000 claims description 4
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 claims description 4
- 230000001580 bacterial effect Effects 0.000 claims description 3
- 238000000605 extraction Methods 0.000 claims description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 2
- 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 claims description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 2
- IKHGUXGNUITLKF-XPULMUKRSA-N acetaldehyde Chemical compound [14CH]([14CH3])=O IKHGUXGNUITLKF-XPULMUKRSA-N 0.000 claims description 2
- 239000011575 calcium Substances 0.000 claims description 2
- 229910052791 calcium Inorganic materials 0.000 claims description 2
- 239000001963 growth medium Substances 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- QNGNSVIICDLXHT-UHFFFAOYSA-N para-ethylbenzaldehyde Natural products CCC1=CC=C(C=O)C=C1 QNGNSVIICDLXHT-UHFFFAOYSA-N 0.000 claims description 2
- 239000011591 potassium Substances 0.000 claims description 2
- 229910052700 potassium Inorganic materials 0.000 claims description 2
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 claims description 2
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 claims description 2
- 239000011734 sodium Substances 0.000 claims description 2
- 229910052708 sodium Inorganic materials 0.000 claims description 2
- HGBOYTHUEUWSSQ-UHFFFAOYSA-N valeric aldehyde Natural products CCCCC=O HGBOYTHUEUWSSQ-UHFFFAOYSA-N 0.000 claims description 2
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical group O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims 3
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 claims 2
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 claims 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims 1
- 239000005711 Benzoic acid Substances 0.000 claims 1
- FERIUCNNQQJTOY-UHFFFAOYSA-N Butyric acid Chemical compound CCCC(O)=O FERIUCNNQQJTOY-UHFFFAOYSA-N 0.000 claims 1
- 235000010233 benzoic acid Nutrition 0.000 claims 1
- WXBLLCUINBKULX-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1.OC(=O)C1=CC=CC=C1 WXBLLCUINBKULX-UHFFFAOYSA-N 0.000 claims 1
- BEFDCLMNVWHSGT-UHFFFAOYSA-N ethenylcyclopentane Chemical compound C=CC1CCCC1 BEFDCLMNVWHSGT-UHFFFAOYSA-N 0.000 claims 1
- 239000004310 lactic acid Substances 0.000 claims 1
- 235000014655 lactic acid Nutrition 0.000 claims 1
- 239000004334 sorbic acid Substances 0.000 claims 1
- 235000010199 sorbic acid Nutrition 0.000 claims 1
- 229940075582 sorbic acid Drugs 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 8
- 239000000047 product Substances 0.000 description 29
- 241000209134 Arundinaria Species 0.000 description 25
- 150000008163 sugars Chemical class 0.000 description 17
- 241000894006 Bacteria Species 0.000 description 10
- 238000004519 manufacturing process Methods 0.000 description 9
- 108090000790 Enzymes Proteins 0.000 description 8
- 102000004190 Enzymes Human genes 0.000 description 8
- 235000012907 honey Nutrition 0.000 description 8
- 244000005700 microbiome Species 0.000 description 7
- 239000007787 solid Substances 0.000 description 7
- 241000192130 Leuconostoc mesenteroides Species 0.000 description 6
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 5
- 239000013078 crystal Substances 0.000 description 5
- 238000002425 crystallisation Methods 0.000 description 5
- 230000008025 crystallization Effects 0.000 description 5
- 230000006378 damage Effects 0.000 description 5
- 239000003381 stabilizer Substances 0.000 description 5
- 229920002307 Dextran Polymers 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 4
- 229930091371 Fructose Natural products 0.000 description 4
- 239000005715 Fructose Substances 0.000 description 4
- RFSUNEUAIZKAJO-ARQDHWQXSA-N Fructose Chemical compound OC[C@H]1O[C@](O)(CO)[C@@H](O)[C@@H]1O RFSUNEUAIZKAJO-ARQDHWQXSA-N 0.000 description 4
- 241000233866 Fungi Species 0.000 description 4
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 4
- 239000008103 glucose Substances 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 239000003899 bactericide agent Substances 0.000 description 3
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 3
- 108010051210 beta-Fructofuranosidase Proteins 0.000 description 3
- 238000010411 cooking Methods 0.000 description 3
- 238000006731 degradation reaction Methods 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 238000003306 harvesting Methods 0.000 description 3
- 238000003801 milling Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 150000001299 aldehydes Chemical class 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000013068 control sample Substances 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 2
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 2
- 230000003628 erosive effect Effects 0.000 description 2
- 238000000227 grinding Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 208000015181 infectious disease Diseases 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000002609 medium Substances 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 239000012452 mother liquor Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 230000006641 stabilisation Effects 0.000 description 2
- 238000011105 stabilization Methods 0.000 description 2
- 210000001519 tissue Anatomy 0.000 description 2
- 241000609240 Ambelania acida Species 0.000 description 1
- 241000193830 Bacillus <bacterium> Species 0.000 description 1
- 235000016068 Berberis vulgaris Nutrition 0.000 description 1
- 241000335053 Beta vulgaris Species 0.000 description 1
- 241000207199 Citrus Species 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 235000005979 Citrus limon Nutrition 0.000 description 1
- 244000131522 Citrus pyriformis Species 0.000 description 1
- 241000186216 Corynebacterium Species 0.000 description 1
- 108010001682 Dextranase Proteins 0.000 description 1
- 241000588698 Erwinia Species 0.000 description 1
- 241000589565 Flavobacterium Species 0.000 description 1
- 241000238631 Hexapoda Species 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 241000607142 Salmonella Species 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 241000219094 Vitaceae Species 0.000 description 1
- 208000027418 Wounds and injury Diseases 0.000 description 1
- 241000589634 Xanthomonas Species 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 238000004500 asepsis Methods 0.000 description 1
- 239000010905 bagasse Substances 0.000 description 1
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid group Chemical group C(C1=CC=CC=C1)(=O)O WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 description 1
- 238000010876 biochemical test Methods 0.000 description 1
- 235000020062 cachaça Nutrition 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000007705 chemical test Methods 0.000 description 1
- 235000020971 citrus fruits Nutrition 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000008121 dextrose Substances 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 210000002615 epidermis Anatomy 0.000 description 1
- 210000000416 exudates and transudate Anatomy 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000013467 fragmentation Methods 0.000 description 1
- 238000006062 fragmentation reaction Methods 0.000 description 1
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- 230000008014 freezing Effects 0.000 description 1
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- 125000002791 glucosyl group Chemical group C1([C@H](O)[C@@H](O)[C@H](O)[C@H](O1)CO)* 0.000 description 1
- 235000021021 grapes Nutrition 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 208000014674 injury Diseases 0.000 description 1
- 229960004903 invert sugar Drugs 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
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- 244000052769 pathogen Species 0.000 description 1
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- 229920001282 polysaccharide Polymers 0.000 description 1
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- 238000004321 preservation Methods 0.000 description 1
- 239000003755 preservative agent Substances 0.000 description 1
- 230000002335 preservative effect Effects 0.000 description 1
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- 235000019260 propionic acid Nutrition 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
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- 238000004062 sedimentation Methods 0.000 description 1
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- 239000002002 slurry Substances 0.000 description 1
- WSWCOQWTEOXDQX-MQQKCMAXSA-N sorbic acid group Chemical group C(\C=C\C=C\C)(=O)O WSWCOQWTEOXDQX-MQQKCMAXSA-N 0.000 description 1
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Abstract
The present invention relates to a product for stabilizing sucrose contained in sugar cane and method of application having pH stabilizing, biochemical, bactericidal, enzymatic, detergent and sanitizing activity consisting of an aqueous solution comprising an active agent, a carboxylic acid or derived salt, a short chain alcohol, terpene, surfactant and a buffer solution whose purpose is mainly to avoid the inversion of saccharo
Description
PRODUCT TO STABILIZE THE SUCROSE CONTAINED IN THE SUGAR CANE AND APPLICATION METHOD.
BACKGROUND
Sucrose is the most important of the sugars, being its primary source the sugar cane and the beet. A large variety of granulated or liquid sugars, honey or invert sugars and brown sugar are obtained from sucrose. (Whistler, R. L., Zysk, J. R. Kirk-Othmer, 3rd ed.Vol 04. 535-555)
The process of obtaining sucrose, also known as sugar from sugarcane is an industrial process of great economic importance, because entire geographical areas of various countries depend heavily on that industry.
It is therefore of great importance the inventions in this field to keep your 2 or operation profitable. That is why innovations have been developed in different parts of the integral production process, which range from sowing, cultivation and harvest to the processing equipment to obtain the final product.
In general terms, the yield of the sugar production process is from 9.2 to 25 12.8% in relation to the sugar cane that arrives for processing in a sugar mill.
This yield varies according to the region, the variety of the sugarcane, the equipment used in the production process, the operating conditions, etc.
The purpose of the sugar factory is to separate all the components that are not sucrose from the cane, to isolate it in the form of crystals. In fact, the cane is divided into its different basic components: fiber, water, no sugar and sucrose.
The cane when entering the factory, is subjected to a process of fragmentation and successive compressions in mills, separating the juice from the fiber. To achieve the greatest possible separation, water is applied to dilute the juice retained by the fiber, which increases the amount of sucrose recovered from sugar cane in this operation.
The juice extracted from sugarcane (commonly referred to as sugarcane juice) has around 15 degrees Brix with a purity that fluctuates between 80 and 90%. Therefore, 100 ton. of juice will contain 15 ton. of total solids and between 12 and 13% polarization (pol.): The amount of non-sugars (impurities) in 100 tons. of juice can then vary between 2 and 3 tons.
The juice of sugar cane is acid, opaque and cloudy. By means of chemical treatment with lime slurry and heating, the acidity is neutralized so that, due to the change in pH and temperature, certain non-sugars, mainly of colloidal nature, which are separated by sedimentation, can be insolubilized and precipitated.
In this way the juice becomes neutral, transparent and clean (clarified juice), but only between 15 and 20% of the total of non-sugars are separated.
The residual product of this process is the cachaça (75% humidity), which represents approximately 3 or 4% of the weight of the cane and contains between 1 and 2% of pol.
In the concentration of the juice -process of evaporation to multiple effect- an amount of water equivalent to 75 or 78% of the weight of the juice is eliminated and it is obtained with a concentration of 65 to 70 brix.
About 80% of the evaporated water is recondensed in the different bodies of the evaporator and is used in the manufacturing processes, mainly in the milling of the cane.
The meladura obtained by concentration of the clarified juice, is subjected to evaporation in vacuum bins, to an appropriate degree of supersaturation so that the sucrose crystallizes; a cooked mass (A) of purity practically equal to that of the meladura is obtained, which contains a quantity of crystals equivalent to 50 or 60% of the total solids. The separation of the sugar is the centrifuge throws as a residual product a mother liquor (honey A) whose purity is 18 points lower than that of the cooked mass. If the purity of this is 85% that of honey will be around 67%. The cooking time of a cooked mass of 40 m3 is about 2 hours.
To the honey (A) a certain quantity of meladura is incorporated to make a cooked mass (B) with 73 or 75 of purity. In this mass the crystals represent 45 to 50% of the total soluble solids present. In the centrifugation, the sugar of a slightly lower quality than (A) is separated, and as a honey residue (B), with an approximate purity of 55%. The greater proportion of impurities in this mass decreases the speed of crystallization and the cooking time in the pan takes about 3 hours.
From the honey (B), enriched with meladura and / or honey (A), the cooked mass (C) of purity is produced around 60%. The yield in glasses with respect to the total solids does not exceed 35 to 40% and the cooking time in the tank can fluctuate between 4 and 8 hours. The high concentration of non-sugars, which include substances capable of imparting high viscosity to the mother liquor, makes this cooked dough a difficult operation with very variable results.
To enable the greatest possible crystallization of sucrose, the cooked mass is subjected to moderate and slow cooling in crystallizers, where it remains between 18 and 36 hours.
From the centrifugation, fine honey with apparent purity between 32 and 40% and sugar (C) of small crystals - about 300 micras - and unsuitable quality for commercialization is obtained. A part of this sugar, mixed with enough meladura to form a magma manageable with a fluid, serves as a crystalline nucleus (seed) for the masses cooked (A) and (B), where its size increases to about 800 microns. The rest is dissolved and incorporated into the meladura.
During the production process there are losses of sucrose contained in sugarcane due to the acidity of the juice, the temperature of the juice and the presence of enzymes in the juice.
These losses, known as sucrose inversion, are caused by a hydrolysis reaction that is effected by an enzymatic action or by the acid hydrogen (pH) potential of the sugarcane juice and the temperature of the juice.
The juice of the cane has a natural acidity which oscillates between 5.0 and 5.70 units, which is a propitious medium for the hydrolysis reaction of sucrose.
The result of the sucrose inversion is glucose and fructose in equal amounts, which are minor sugars with characteristics different from sucrose.
This type of minor sugars do not have greater economic interest for the mills. The mixture of these sugars is also known as "invert sugar".
The fructose maintains its liquid state in the process of obtaining sucrose, so it is also known as non-crystallizable sugars.
The other product of the degradation of sucrose either by deterioration in the field or in the factory is glucose or also called dextrose, which has the characteristic of giving high readings of sucrose, which leads to register more sucrose than it really is crystallizable, thus causing economic losses to the mill, to pay for sucrose that can not be recovered.
The normal temperature of the cane juice initially extracted is sufficiently low, so that the investment caused by the heat is minimal. However, the temperature of the juice is increased in subsequent stages of the process, which favors the inversion of sucrose.
In the initial stage the effect of enzymes is the main factor that causes the inversion of sucrose.
Enzymes are presented by the growth and proliferation of bacteria, which are practically unavoidable since sugar cane is a material that drags a large number of foreign agents into the grinding stage, ranging from natural salts of the earth to organic matter and microorganisms.
Some sugar mills use bactericides to eliminate the bacteria contained in sugarcane juice. However, bactericidal products do not act on enzymes or on minor sugars.
The microbial content of uncut sugar cane is variable, being influenced mainly by temperature, humidity and climatic conditions.
Microorganisms can develop on the surface or in the joints of the leaves with the stem, invade erosions of the epidermis or healthy tissues and cause diseases in the plant.
The leaves and trunks of the plant contain bacteria, yeast and fungi. The 0 microbial populations of the cane leaves infected by bacteria, fungus and viruses are greater than those of healthy canes.
The bacterial species that are most frequently found in the leaves and normal stems are flavobacterium, xanthomonas, enterbacter, dseudomonas, erwinia, 5 leuconostoc mesenteroides, bacillus and corynebacterium, yeast and fungi. Some of these are potentially pathogenic species for plants.
The bark of the cane can be injured by the action of insects or crack due to the growth, freezing or burning of the leaves, the exudates that appear or on the surface, or the tissues that are invaded through these erosions, offer ecosystems suitable for the growth of different bacteria, yeasts and fungi. However, in order to develop, they must concur to other factors such as the extent of the physical damage, the existing temperature and the time that elapses between the injury and the harvesting of the cane. 5 It is proven by experiments in the field that the burning of sugarcane leaves can not destroy the bacteria present in the cane.
Enzymes are generated by bacteria, microorganisms and even by the plant itself.
These enzymes act as a crystallizer that accelerates the reaction of the inversion of sucrose.
Rapidly growing yeasts, molds and bacteria secrete the invertase enzyme to obtain the food supply required for their growth and reproduction, because these microorganisms can not directly metabolize sucrose. So the action of the invertase enzyme is formed glucose and fructose, which can be used as a supply of coal and the energy required by microorganisms.
The enzyme invertase is not consumed during the time of inversion but remains in the juice causing destruction of additional sucrose.
To deactivate the enzymes it is necessary to subject them to temperatures of the order of 60-70 ° C for a period of approximately one hour, but in any case only 50% of their activity is eliminated.
The juice of the cane is usually a means of ideal conditions for the growth and development of microorganisms, which when coming into contact with the equipment and suspended solids form slats that adhere to the metal walls giving rise to colonies of billions of microorganisms , which in some cases have the capacity to double its population every 20 minutes, with the consequent destruction of sucrose present in the juice of the cane.
Another sucrose loss of significant proportions occurs when the bacterium Leuconostoc mesenteroides, which has the property of reproducing extremely rapidly in the normal conditions of the juice extracted from the cane by grinding and without heating; It is able to produce large amounts of dextran from glucose and fructose. 5 When the presence of Leuconostoc mesenteroides in the cane juice is in counts higher than 1000 mg / kg (solids), the formation of said dextrans -polysaccharides of high molecular weight- considerably increases the viscosity of the sugar solutions; and during the evaporation the concentration of dextrans increases later reflecting 0 in the stage of crystallization where it causes that masses are obtained of low purity giving rise to disorders in the crystallization producing amorphous sugar crystals, which give a bad aspect from the point of view commercial.
To eliminate the bacteria, the commonly known bactericides are applied, but still there is a loss of purity ranging between 4 and 8% of the sucrose content.
This and the other effects described above greatly influence the economic results of the sugar mill harvest.
o These sucrose losses are considered normal since there is no way to prevent them until now.
It is therefore the object of the present invention to provide a product that allows to preserve the purity of the sugarcane juice and stabilizer of the sucrose contained in the sugarcane through the separation and purification process.
A further object of the present invention is to apply a product at any stage of the sugar production process from sugarcane to prevent sucrose from degrading.
Still another object of the present invention is to provide a product that reduces the problems of fouling of material in the pipes of conduction and in the equipment of process in a sugar mill.
Another object of the present invention is to provide a product that eliminates the use of bactericidal agents.
DETAILED DESCRIPTION OF THE INVENTION.
The applicant has developed a product and method of application that stabilizes the sucrose contained in sugarcane and that retains the properties of cane juice similar to that of fresh juice as it is processed, which prevents the degradation of the sucrose contained in sugarcane during its process of separation of the rest of the materials of the cane for its bactericidal effects, stabilization of the pH and its activity on the enzymes that cause the degradation process of sucrose.
The product consists of an aldehyde solution in a range of 35-40% by weight concentration, to which a carboxylic acid of one to eight carbons or one of its salts is added by mixing until a maximum proportion of 15% is obtained. by weight, additionally an alcohol of up to eight carbons can be added in a proportion between 5 to 15% by weight and optionally 1 to 2% by weight of terpene with a surfactant to solubilize the terpenes of between 0.2 and 2% by weight and up to 2% of a buffer solution.
The aldehyde can be chosen from the group consisting of formaldehyde, formaldehyde, acetaldehyde, propionaldehyde, butyraldehyde and benzaldehyde.
The carboxylic acid is preferably propionic acid or one of the following acids: formic, acetic, propionic, butanoic, benzoic, sorbic or lactic, or some of its corresponding salts, preferably sodium, potassium, calcium, magnesium and ammonium ions.
The product preferably contains an alcohol selected from the following: 0 methanol, ethanol, propanol, butanol, pentanoi, hexanol, heptanol, octanol or phenol.
Terpene is a compound of vegetable origin, extracted from sunflower seeds, grapes, lemon or some other citrus.
The buffer solution consists basically of a culture medium of bacteria such as salmonella.
The product obtained is applied in a range of 25 to 75 ppm per ton of sugarcane in process at any stage of the production process by means of a continuous flow meter.
The product can be applied in different stages of the process, for example it can be directly by spraying or other method to the cane since it is harvested or when it reaches the mill for processing, or by means of dosers to the juices of the first 5 extraction , mixed juices or clarified juice.
To make better use of its various effects, it is preferably applied to the juices of the first extraction, although depending on the specific conditions of the mill it can also be applied at other points of the process, and even at several points simultaneously if necessary.
The product exerts a samtizante effect in the possible foci of infection of the general system. This is directly reflected in the increase in the percentage of recovery and facilitates maintenance work.
The effectiveness of the product was evaluated in the laboratory of a sugar mill. To do this, the following experiment was prepared: three samples of the cane juice obtained by milling the sugarcane in eight different operating times of the mill were taken. For each case, the purity of the cane juice and the percentage of reducing sugars were determined, according to the practices commonly used. One sample was left as a control, another was added the equivalent of 35-40 ppm of the stabilizer product per ton of sugarcane, and the third was added 50-65 ppm of the stabilizer product per ton of cane.
Subsequently the two variables were determined again to the three samples at four and eight hours. The results of the experiment are summarized in the following two tables.
The first results correspond to the determination of the purity, that is to say the amount of sucrose that is preserved for its recovery in subsequent stages.
It can be seen that the values of the purity of the samples in which the sucrose stabilizing product was applied, in general terms, are greater than that of the control sample.
With respect to the determination of the reducing sugars, which are waste or unwanted contaminants, the following results were obtained.
In these cases it is also observed that in a general way the amount of reducing sugars that are produced in the samples to which the sucrose stabilizing product is added is lower than that of the control sample.
To verify the results of the industrial purity stabilizer product, an application test was carried out for eight days in a sugar mill with the capacity to process 204 tons. per day and with a percentage recovery of sucrose of 93%.
A continuous flow doser was used to supply the product in a proportion 5 of 40-60 ppm per tonne of equivalent cane.
It was observed and verified several chemical and biochemical tests that the product acted as a biochemical agent in a range of broad spectrum and in periods of up to 18 hours, efficiently inhibited the destruction of sucrose, maintaining its greater effectiveness or within a temperature range of 50 to 95 ° C.
With the application of the stabilizing and preservative product, the purity of the juices is adequately maintained, that is, that the sucrose was not degraded.
It could also be observed that the product acts biochemically on the non-crystallizable sugars contained in sugarcane juice, which can originate mainly when there is lag, deterioration and / or deficient asepsis in the equipment of the batey and milling areas.
o The product also showed an inhibitory effect of the bacterium Leuconostoc mesenteroides present in the juices of sugarcane. In addition to interacting with the minor sugars produced by the action of the bacteria Leuconostoc mesenteroides, reducing the viscosity of the masses cooked by transforming said gums, waxes, resins and starches into manageable materials. 5 A detergent action was shown that facilitates the handling of the materials in process and avoids negative interferences in the crystallization stage, achieving a good formation of the sugar grain. These effects represent a reduction in the work and therefore in the maintenance and cleaning costs of the process equipment.
The preservation of sucrose from cane juice as a consequence of the inhibition of the bactericidal activity of Leuconostoc mesenteroides, of the stabilization of the hydrogen potential (PH) in the juice, as well as the enzymatic activity of dextranase on the dextran present in juices, makes the ratio of the amount of sucrose preserved to the totality of dissolved solids in the juice remain more or less stable within a range that depends on the amount of sucrose and the bacterial population present in the medium concerned.
The product develops a sanitizing effect in the centers of infection of the mill, which allows to achieve an additional increase in the recovery of sugar per ton of ground cane, facilitating also a better handling of the materials in the production process, reducing the dead times to act in places that are not accessible to routine cleaning actions.
In this particular mill, 21 to 25 tons of sucrose were obtained in addition to those produced in the traditional way.
The loss of sucrose in the residual juice went from 5.88 to 3.73% and in bagasse from 3.66 to 3.25% with the application of the product and process object of the present invention. With the application of the stabilizer product, the loss of sucrose was only 4%, that is, 4 points less than the current.
Claims (4)
1. A product for stabilizing sucrose contained in sugarcane and application method having pH, biochemical, bactericidal, enzymatic, detergent and sanitizing stabilizing activity consisting of an aqueous solution comprising from 15 to 40% of an active agent, 5 to 15% of a carboxylic acid or derived salt, 5 to 15% of a short chain alcohol, 1 to 2% terpene, and up to 2% of a buffer solution.
2. A product for stabilizing the sucrose contained in the sugar cane and method of application, according to clause 1, wherein said active agent consists of formaldehyde, formaldehyde, acetaldehyde, propionaldehyde, butyraldehyde or benzaldehyde or a mixture of some of them.
3. A product to stabilize the sucrose contained in the sugar cane and method of application, according to clauses 1 and 2, where the active agent is preferably formaldehyde in a proportion of 35 to 40%.
4. A product for stabilizing the sucrose contained in the sugar cane and method of application, according to clause 1, wherein the carboxylic acid consists of formic, acetic, propionic, butanoic, benzoic, sorbic or lactic acid. A product to stabilize the sucrose contained in the sugar cane and method of application, in accordance with clauses 1 and 4, where the carboxylic acid can be substituted by a corresponding salt, preferably sodium, potassium, calcium and ammonium ions. A product for stabilizing the sucrose contained in the sugar cane and method of application, according to clause 1, wherein the short chain alcohol consists of methanol, ethanol, propanol, butanol, pentanoi, hexanol, heptanol, octanol or phenol. A product to stabilize the sucrose contained in the sugar cane and method of application, according to clause 1, where the buffer solution consists of a bacterial culture medium. A product to stabilize the sucrose contained in the sugar cane and method of application, according to clauses 1 to 7, characterized in that the product can be applied to the material in process in a sugar mill at any stage. A product for stabilizing the sucrose contained in the sugar cane and method of application, according to clauses 1 to 8, characterized in that the product is preferably applied to the juice of the first extraction. A product to stabilize the sucrose contained in the sugarcane and application method, in accordance with clauses 1 to 9, characterized in that the product is preferably applied in a proportion of 25 to 75 ppm per ton of sugarcane entering the sugar cane. process in a sugar mill. A product to stabilize the sucrose contained in the sugarcane and application method, in accordance with clauses 1, where 0.2 to 2% of a suitable surfactant is optionally applied to solubilize the terpene.
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| MXPA/A/1996/001323A MXPA96001323A (en) | 1996-04-08 | Product to stabilize the sucrose contained in the sugar cane and application method | |
| AU25777/97A AU2577797A (en) | 1996-04-08 | 1997-04-08 | Process and product for stabilizing the saccharose contained in sugar cane |
| GT199700040A GT199700040A (en) | 1996-04-08 | 1997-04-08 | PRODUCTS TO STABILIZE THE SUCROSE CONTAINED IN SUGAR CANE AND METHOD OF APPLICATION |
| PCT/MX1997/000009 WO1997038017A1 (en) | 1996-04-08 | 1997-04-08 | Process and product for stabilizing the saccharose contained in sugar cane |
| CO97017876A CO4600663A1 (en) | 1996-04-08 | 1997-04-08 | PRODUCT TO STABILIZE THE SUCROSE CONTAINED IN SUGAR CANE AND METHOD OF APPLICATION |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| MXPA/A/1996/001323A MXPA96001323A (en) | 1996-04-08 | Product to stabilize the sucrose contained in the sugar cane and application method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| MX9601323A MX9601323A (en) | 1998-08-30 |
| MXPA96001323A true MXPA96001323A (en) | 1998-11-12 |
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