Patent Application
20110277751
The present invention relates to a process for manufacturing sugar from sugarcanes.
In India, sugar is manufactured by a conventional double sulfitation process from sugarcane.
In the second step, the prepared sugarcane is fed to cutter and then chopped and fed along with juice through a series of milling tandems (herein after referred to as mill). This step is known as milling where juice is extracted from the bagasse. Generally, milling comprises four or five mills in series. Normally, hot water is used in the last mill for maximum extraction of the juice from bagasse and juice collected is added in the previous mill. During milling, aqueous solutions of Chlorine, Iodine, Quaternary ammonium compounds, corbomate or dithiscorbonate based may be added for cane sanitation.
The juice obtained from mills is then passed through a series of juice heater for better reaction of juice with lime. In the 1st juice heater, juice is heated at about temperature of 70° C. However, heating of juice changes microbiology of the juice, where microbes having capacity to grow at a high temperature initiates their growth and microbes growing at normal temperature either die or remain in dormant stage till favorable conditions return.
The heated juice is then treated with milk of lime to raise pH above 9 or desired level to facilitate precipitation of inorganic impurities which is immediately followed by treatment with SO2 gas released from sulfur burner in a sulfitation tower to reduce to a pH of juice to about 7.0 and decolorization. This is a FIRST SULFITATION step. Phosphoric acid may be added to the juice if sugarcane does not have sufficient phosphate content. The sulfited juice is passed through heater again to raise temperature to about 105° C. The heated juice is then sent to settling tank/clarifier (herein after referred to as Dorr settler). Flocculants and allied chemicals are added to promote flocculation and settling of mud and impurities in the Dorr settler. Juice overflowing from Dorr is clear and free from suspended impurities, which is then send through to series of evaporators to boil off water for further concentration to obtain concentrated juice of about 60% solids (brix) which is called as syrup. This syrup is again treated with SO2 gas to decolorize the syrup and is sent to further concentration and crystallization in crystallizers and pans. This is SECOND SULFITATION step. This sulfated syrup has generally acidic pH about 5.0-5.5 and remaining process is thus carried with acidic pH. The liquor containing solid sugar from Pans dropped in centrifuge where sugar is separated from mother-liquor (molasses) by centrifugal force and is washed with steam and/or hot water. Sugar separated is the final product which is bagged after drying on through hoppers and silo. Petrochemical base or polymer base such as DOSS, NP10, surfactants as viscosity reducers may be used to reduce viscosity as a pan aid agent. This sugar contains sulfur dioxide, lead, conductivity ash, reducing sugar and moisture along with sucrose. The specifications of such plantation white sugar are as follows:
The sulfur treatment on juice and syrup is carried out mainly for decolorizing juice and syrup. The sulfur treatments along with mill sanitation as described above also help to reduce microbial activity. However, as sulfitation and mill sanitation only reduces microbial activity to certain extent and sugar loss due to microorganisms/microbes takes place during the process resulting in loss in the final yield of the sugar. Further, in the last stage of the process, syrup has an acidic pH which results in further loss of the sugar. Moreover, the sugar produced by this method contain significant amount of sulfur (SO2) content i.e. 50-70 ppm, significant level of impurities and has acidic pH, therefore, not good for human health also. Furthermore, sugar produced by above double sulfitation process looses its color in storage as bleaching effect of sulfur (SO2) reduces with time. Sugar with higher SO2 and lower pH has limited keeping quality or in other words, quality of sugar deteriorates significantly during storage, that is, the sugar produced by this process has lower shelf life.
Further, day by day cost of Sulfur is also increasing resulting in the increasing the expenses of the double sulfitation process.
One of the main objects of the present invention is to provide a sugar manufacturing process to minimize or discontinue use of sulfur.
Further object of the present invention is to reduce the loss of sugar due to microbial activity.
Furthermore object of the present invention is to provide a sugar manufacturing process to reduce impurities in the sugar.
Further, another object of the present invention is to provide a process for manufacturing sugar to overcome shortcomings of the double sulfitation process.
The present invention provides a method for manufacturing sugar, which short-circuits at least one sulfitation step and utilizes means for minimizing microbe/microorganism activity.
The present invention provides a method for manufacturing sugar from sugarcane, comprising steps of dosing biocides on sugarcane during cane preparation and milling to kill about 90% microbes including microbes growing at high temperature; heating juice obtained from the mills at about 70 deg. C.; neutralizing the juice; heating the neutralized juice to about 105 deg C.; passing the heated juice through clarifiers or settling tanks; evaporating to boil-off water to obtain syrup of the juice having about 60% solids; crystallizing the syrup; and separating, washing and drying the sugar; wherein sugar produced is about neutral and contains substantially lower amount of sulfur.
In one embodiment, the neutralizing step of the method comprises step of mixing of the lime with the juice to neutralize the juice to produce sugar having substantially zero amount of sulfur.
In another embodiment, the neutralizing step includes raising pH of the juice to about 7.5-8.0 by mixing lime and mixing phosphoric acid and/or carbon dioxide (CO2) and/or SO2 to neutralize the alkaline juice to produce sugar having substantially less or zero amount of sulfur.
In further embodiment, the neutralizing step includes treating juice with milk of lime to raise pH above 9 or desired level to facilitate precipitation of inorganic impurities and neutralizing the alkaline juice with carbon dioxide (CO2) to produce sugar having substantially zero amount of sulfur.
In one another embodiment, the neutralizing step includes treating juice with milk of lime to raise pH above 9 or desired level to facilitate precipitation of inorganic impurities and neutralizing the alkaline juice with sulfur dioxide (SO2) to produce sugar having low amount of sulfur.
According to one embodiment of the present invention, the biocide sprayed or added during cane sanitation or mill sanitation is aqueous formulation of Formula I comprising: mixture of synergistically acting solutions of sodium and/or potassium salts of methyl,&/or dimethyl, &/or ethyl &/or cyanodiethyl dithiocarbamates about 25-50% w/w preferably 40±0.5% w/w, and 0 to 10 parts of foaming or non-foaming type dispersant/chelating agent formulated to kill about 90% microbes in ten minute. The Formula I biocide is preferably added in the milling step.
According to another embodiment, the biocide sprayed or added during cane sanitation or mill sanitation is aqueous formulation of Formula II comprising: mixture of synergistically acting solutions of sodium and/or potassium salts of methyl,&/or dimethyl, &/or ethyl &/or cyanodiethyl dithiocarbamates about 25-50% w/w preferably 40±0.5% w/w; one or in combination of amine based, polymer based, phosphate based, phosphonate based, organosulfur based, quinine based chelating/sequestrating/penetrating compound about 0.01 to 5% w/w; and 0 to 10 parts of foaming or non-foaming type dispersant/chelating agent formulated to kill about 90% microbes in one minute. The Formula II biocide is preferably added in the cane preparation step.
The present invention also provides amine polymer which may be added continuously, if necessary, to the juice or syrup for removal of impurities from sugar crystals at the time of crystallization in a quantity preferably 10 ppm and can vary from 2-20 ppm depending upon the quality of juice and/or syrup or to obtain desired quality of sugar. Also, if necessary, viscosity reducers such as various glycols, amines, acetates and/or non ionic polymer may be added continuously with suitable dilution to the syrup to reduce viscosity and improve crystallization and washing of sugar in centrifuge.
According to the present invention, viscosity reducers and flocculants may be added.
Reference made to embodiments of the invention discussed above with objectives, examples of which may be illustrated in the accompanying figures. These figures are intended to be illustrative, not limiting. Although the embodiments of the invention are generally described in the context of these drawings, it should be understood that it is not intended to limit the scope of the embodiments of the invention to these drawings, in which:
Various embodiments of this invention provide a method for manufacturing sugar from sugarcane. However, the embodiments are not limited and may be used in connection with various applications that will be described in later part of this specification.
In general, the present invention provides an improved method for manufacturing sugar which includes steps of spraying or adding or dosing biocides during cane preparation (calling as cane sanitation) and milling (calling as mill sanitation), short-circuiting at least one or both sulfitation steps of the conventional double sulfitation process and then treating sugarcane juice/syrup with two new formulations such as viscosity reducer and amine-based polymer for improving crystallization and for removing impurities, including decolorization of the sugar.
The present invention utilizes two biocide formulations, namely Formula I and Formula II, to kill the microbes during cane sanitation and mill sanitation step.
According to the present invention, the biocide of Formula I comprises mixture of synergistically acting solutions of sodium and/or potassium salts of methyl &/or dimethyl, &/or ethyl &/or cyanodiethyl dithiocarbamates about 25-50% w/w preferably 40±0.5% w/w, and 0 to 10 parts of foaming or non-foaming type dispersant/chelating agent formulated to kill about 90% microbes in ten minute.
According to the present invention, the biocide of Formula II comprises mixture of synergistically acting solutions of sodium and/or potassium salts of methyl,&/or dimethyl, &/or ethyl &/or cyanodiethyl dithiocarbamates about 25-50% w/w preferably 40±0.5% w/w; one or in combination of amine based, polymer based, phosphate based, phosphonate based, organosulfur based, quinine based chelating/sequestrating/penetrating compound about 0.01 to 5% w/w; and 0 to 10 parts of foaming or non-foaming type dispersant/chelating agent formulated to kill about 90% microbes in one minute.
As shown in
Then, in the milling step, the shredded and fibrillated cane is fed to mills to remove and extract juice from the cane wherein the biocides of Formula I is added to kill about 90% microbes including microbes capable of growing at high temperature in ten minute. In milling, the Formula I biocide is added or dosed in aqueous form and can be added in one of the mills or may be split into more places or in juice collecting tanks or the last two or three mills for mill sanitation. The adding or dosing of the biocide of the Formula I depends upon cane quality and environmental factor such as temperature, humidity, rainfall during harvesting/crushing. Generally, the total dose may vary from 1 ppm to 20 ppm and preferable dose is 10 ppm.
As shown in
According to the first embodiment to the invention, juice can be neutralized by mixing of the lime with the juice i.e. adding lime to neutralize the acidic juice.
In the second embodiment of the present invention, juice can be neutralized by initially raising pH of the juice to about 7.5-8.0 by mixing lime and then mixing phosphoric acid and/or CO2 to neutralize the alkaline juice.
In the third embodiment, according to the present invention the juice can be neutralized by treating the juice first with milk of lime to raise pH above 8 or at desired level and neutralizing the alkaline juice with SO2 by using sulfur burner.
According to the forth embodiment of the present invention, CO2 gas can be used in the third embodiment to neutralize the alkaline juice instead of SO2 to avoid sulfur content in the final product.
As shown in
The present invention provides amine polymer of formula III that can be added continuously, if necessary, to the juice and/or syrup for removal of impurities from sugar crystals at the time of crystallization. The total dose of the Formula III varies from 2-20 ppm and preferable dose is 10 ppm.
Formula III is aqueous solution of polymer active matter of 20 to 60% preferably 45% made by reacting coco di-methyl amine/alkyl amine with epi-chlorohydrine in a reaction vessel. The process consists steps of adding 10-40 parts of coco di-methyl or alkyl amine with continuous stirring, cooling and adding 8 to 42 parts of epi-chlorohydrine slowly to carry out reaction between 25-60 deg C., and then transferring the milky white reaction mixture in air tight containers and allowing reaction mixture to become a translucent viscous liquid. Other agents such as color precipitants and/or flocculants may be added depending on the requirement.
The present invention also provides a chemical formulation of Formula IV comprising various glycols, amines, acetates and/or non ionic polymer in predetermined ratio that may be added continuously with suitable dilution, if necessary, to the syrup as viscosity reducer so as to achieve reduced viscosity of syrup, which would favor better and faster crystallization. The dose of the viscosity reducer may vary from 1 ppm to 20 ppm depending on the viscosity of the syrup and recommended dose is 5 ppm.
Formula IV viscosity reducer consists of at least:
The sugar produced using process of the present invention has microbial-count less than 200 cfu per 10 gm of sugar and lower impurities such as dextran, calcium, conductivity ash. Further, sugar also has acceptable lower color and lower moisture.
The neutralizing processes described in first, second and forth embodiments completely eliminate use of the SO2 i.e. eliminate sulfitation process leading into zero percent of sulfur in the final product.
The neutralizing process describes in the third embodiment avoids use of the SO2 treatment of syrup in second stage, thereby resulting significant reduction in sulfur content in the sugar. This process can be called as single sulfitation process.
Sugar manufactured by above mentioned process has pH of sugar about neutral and improved shelf life. Sugar obtained by the present invention is beneficial for health-conscious people because of its unique features, namely, the extremely low microbial count and negligible or zero sulfur content. Further, impurities like conductivity ash, dextran, calcium, reducing sugar etc are less in the sugar produced by present invention than that of by conventional invention.
The present invention will now be further explained in the following examples. However, the present invention should not be construed as limited thereby. One of ordinary skill in art will understand how to vary the exemplified preparation to obtain the desired results.
The method described in third embodiment is carried out at Kisanveer Satara Sahaksri Sakhar Karkhana Ltd., Bhuinj as an experiment. The quantity of raw material used is as follows:
As against the specifications results achieved by this process, the sugar was sent for analysis to Maarc Labs, Pune (an ISO 17025 lab accredited by NABL). The results are as follows:
Microbial count: 120 cfu per 10 g
SO2 content: >2 ppm
pH: 6.6
The method described in first embodiment is carried out at Kisanveer Satara Sahakari Sakhar Kharkhana Ltd., Bhuinj as an experiment. The quantities of raw material used are as follows:
The sugar produced was sent to United Sugar Company, Saudi Arabia for analysis. As against the specifications results achieved by this process are as follows:
The sugar produced by single sulfitation process contains less amount of sulfur i.e. less than 2 ppm and sugar produced by a process without sulfitation contain negligible amount of sulfur.
While the present invention has been disclosed in connection with certain embodiments, this description should not be taken as limiting the invention to all of the provided details. Modifications and verifications of the described embodiments may be made without departing from the scope and spirit of the invention. Various multiple alternate embodiments are encompassed in the present invention disclosure would be understood by one f ordinary skill in the art. The scope of the invention is to be limited only by the following claims:
| Number | Date | Country | Kind |
|---|---|---|---|
| 754/MUM/2007 | Aug 2007 | IN | national |
| 868/MUM/2008 | Apr 2008 | IN | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/IN08/00501 | 8/11/2008 | WO | 00 | 2/8/2010 |
