Method for purifying beet juice using recycled materials

A method for treating and purifying beet juice using recycled lime and recycled calcium carbonate compositions comprising the steps of:

• providing a supply of beet juice comprising water, sugar, and dissolved non-sugar impurities therein;
• combining said beet juice with a preliminary supply of lime and a preliminary supply of calcium carbonate in a preliming chamber in order to produce a first juice fraction and a second juice fraction, said second juice fraction comprising a plurality of solid floc particles therein, said floc particles being formed from said non-sugar impurities in said beet juice when said preliminary supply of lime and said preliminary supply of calcium carbonate are combined with said beet juice;
• separating said first juice fraction from said second juice fraction;
• combining said second juice fraction with a primary supply of carbon dioxide gas in a primary carbonation chamber in order to remove said preliminary supply of lime from said second juice fraction, said combining of said second juice fraction and said primary supply of carbon dioxide gas producing a calcium carbonate reaction product in said second juice fraction, said calcium carbonate reaction product encapsulating said solid floc particles within said second juice fraction;
• removing said calcium carbonate reaction product and said floc particles encapsulated by said calcium carbonate reaction product from said second juice fraction;
• recombining said first juice fraction and said second juice fraction in order to produce a third juice fraction;
• combining said third juice fraction with a main supply of lime in a main liming chamber in order to degrade remaining amounts of said dissolved non-sugar impurities which are present within said third juice fraction;
• combining said third juice fraction with a secondary supply of carbon dioxide gas in a secondary carbonation chamber in order to remove said main supply of lime therefrom, said combining of said third juice fraction with said secondary supply of carbon dioxide gas producing a calcium carbonate sludge product within said third juice fraction, said calcium carbonate sludge product adsorbing residual amounts of said dissolved non-sugar impurities which are present within said third juice fraction, said secondary carbonation chamber being maintained separately from said primary carbonation chamber;
• removing said calcium carbonate sludge product from said third juice fraction in order to produce a treated juice product;
• dividing said calcium carbonate sludge product into a calcium carbonate-containing first sludge portion and a calcium carbonate-containing second sludge portion;
• routing said first sludge portion into said preliming chamber for use as said preliminary supply of calcium carbonate in treating additional quantities of beet juice materials which enter said preliming chamber;
• heating said second sludge portion to a temperature of about 980.degree.-1200.degree. C. to convert said second sludge portion into a supply of regenerated lime and a gaseous reaction product comprising carbon dioxide therein;
• routing said regenerated lime into said main liming chamber for use as said main supply of lime in treating additional quantities of beet juice materials which enter said main liming chamber;
• and
• routing said gaseous reaction product into at least one of said primary carbonation chamber and said secondary carbonation chamber for use therein.

A method for treating and purifying beet juice using recycled lime and recycled calcium carbonate compositions comprising the steps of:

• providing a supply of beet juice comprising water, sugar, and dissolved non-sugar impurities therein;
• heating said beet juice to a temperature of about 65.degree.-85.degree. C;
• combining said beet juice with a preliminary supply of lime and a preliminary supply of calcium carbonate in a preliming chamber in order to produce a first juice fraction and a second juice fraction, said second juice fraction comprising a plurality of solid floc particles therein, said floc particles being formed from said non-sugar impurities in said beet juice when said preliminary supply of lime and said preliminary supply of calcium carbonate are combined with said beet juice, said preliminary supply of lime being combined with said beet juice in an amount sufficient to cause said beet juice to have a pH level above about 11.6;
• separating said first juice fraction from said second juice fraction;
• combining said second juice fraction with a primary supply of carbon dioxide gas in a primary carbonation chamber in order to remove said preliminary supply of lime from said second juice fraction, said combining of said second juice fraction and said primary supply of carbon dioxide gas producing a calcium carbonate reaction product in said second juice fraction, said calcium carbonate reaction product encapsulating said solid floc particles within said second juice fraction;
• removing said calcium carbonate reaction product and said floc particles encapsulated by said calcium carbonate reaction product from said second juice fraction;
• recombining said first juice fraction and said second juice fraction in order to produce a third juice fraction;
• heating said third juice fraction to a temperature of about 85.degree.-90.degree. C.;
• combining said third juice fraction with a main supply of lime in a main liming chamber in order to degrade remaining amounts of said dissolved non-sugar impurities which are present within said third juice fraction, said main supply of lime being combined with said third juice fraction in an amount sufficient to cause said third juice fraction to have a pH level above about 12.6;
• combining said third juice fraction with a secondary supply of carbon dioxide gas in a secondary carbonation chamber in order to remove said main supply of lime therefrom, said combining of said third juice fraction with said secondary supply of carbon dioxide gas producing a calcium carbonate sludge product within said third juice fraction, said calcium carbonate sludge product adsorbing residual amounts of said dissolved non-sugar impurities which are present within said third juice fraction, said secondary carbonation chamber being maintained separately from said primary carbonation chamber;
• removing said calcium carbonate sludge product from said third juice fraction in order to produce a treated juice product;
• dividing said calcium carbonate sludge product into a calcium carbonate-containing first sludge portion and a calcium carbonate-containing second sludge portion, said dividing of said calcium carbonate sludge product comprising removing about 5-30% by weight of said calcium carbonate sludge product as said first sludge portion, and removing about 70-95% by weight of said calcium carbonate sludge product as said second sludge portion;
• routing said first sludge portion into said preliming chamber for use as said preliminary supply of calcium carbonate in treating additional quantities of beet juice materials which enter said preliming chamber;
• heating said second sludge portion to a temperature of about 980.degree.-1200.degree. C. in order to convert said second sludge portion into a supply of regenerated lime and a gaseous reaction product comprising carbon dioxide therein;
• adding a supply of extra lime to said supply of regenerated lime;
• routing said regenerated lime into said main liming chamber for use as said main supply of lime in treating additional quantities of beet juice materials which enter said main liming chamber;
• and
• routing said gaseous reaction product into at least one of said primary carbonation chamber and said secondary carbonation chamber for use therein.

A method for treating and purifying beet juice using recycled lime and recycled calcium carbonate compositions comprising the steps of:

• providing a supply of beet juice comprising water, sugar, and dissolved non-sugar impurities therein;
• combining said beet juice with a preliminary supply of lime and a preliminary supply of calcium carbonate in a preliming chamber in order to produce a first juice fraction and a second juice fraction, said second juice fraction comprising a plurality of solid floc particles therein, said floc particles being formed from said non-sugar impurities in said beet juice when said preliminary supply of lime and said preliminary supply of calcium carbonate are combined with said beet juice;
• separating said first juice fraction from said second juice fraction;
• combining said second juice fraction with a primary supply of carbon dioxide gas in a primary carbonation chamber in order to remove said preliminary supply of lime from said second juice fraction, said combining of said second juice fraction and said primary supply of carbon dioxide gas producing a calcium carbonate reaction product in said second juice fraction, said calcium carbonate reaction product encapsulating said solid floc particles within said second juice fraction;
• removing said calcium carbonate reaction product and said floc particles encapsulated by said calcium carbonate reaction product from said second juice fraction;
• recombining said first juice fraction and said second juice fraction in order to produce a third juice fraction;
• combining said third juice fraction with a main supply of lime in a main liming chamber in order to degrade remaining amounts of said dissolved non-sugar impurities which are present within said third juice fraction;
• combining said third juice fraction with a secondary supply of carbon dioxide gas in a secondary carbonation chamber in order to remove said main supply of lime therefrom, said combining of said third juice fraction with said secondary supply of carbon dioxide gas producing a calcium carbonate sludge product within said third juice fraction, said calcium carbonate sludge product adsorbing residual amounts of said dissolved non-sugar impurities which are present within said third juice fraction said secondary carbonation chamber being maintained separately from said primary carbonation chamber;
• removing said calcium carbonate sludge product from said third juice fraction in order to produce a treated juice product;
• dividing said calcium carbonate sludge product into a calcium carbonate-containing first sludge portion and a calcium carbonate-containing second sludge portion;
• routing said first sludge portion into said preliming chamber for use as said preliminary supply of calcium carbonate in treating additional quantities of beet juice materials which enter said preliming chamber;
• converting said second sludge portion into a supply of regenerated lime, said converting of said second sludge portion into said regenerated lime comprising heating said second sludge portion to a temperature sufficient to produce said regenerated lime from said second sludge portion;
• dividing said supply of regenerated lime into a first lime fraction and a second lime fraction;
• routing said first lime fraction into said main liming chamber for use as said main supply of lime in treating additional quantities of beet juice materials which enter said main liming chamber;
• and
• routing said second lime fraction into said preliming chamber for use as said preliminary supply of lime in treating additional quantities of beet juice materials which enter said preliming chamber.

A method for treating and purifying beet juice using recycled lime and recycled calcium carbonate compositions comprising the steps of:

• providing a supply of beet juice comprising water, sugar, and dissolved non-sugar impurities therein;
• combining said beet juice with a preliminary supply of lime and a preliminary supply of calcium carbonate in a preliming chamber in order to produce a first juice fraction and a second juice fraction, said second juice fraction comprising a plurality of solid floc particles therein, said floc particles being formed from said non-sugar impurities in said beet juice when said preliminary supply of lime and said preliminary supply of calcium carbonate are combined with said beet juice;
• separating said first juice fraction from said second juice fraction;
• combining said second juice fraction with a primary supply of carbon dioxide gas in a primary carbonation chamber in order to remove said preliminary supply of lime from said second juice fraction, said combining of said second juice fraction and said primary supply of carbon dioxide gas producing a calcium carbonate reaction product in said second juice fraction, said calcium carbonate reaction product encapsulating said solid floc particles within said second juice fraction;
• removing said calcium carbonate reaction product and said floc particles encapsulated by said calcium carbonate reaction product from said second juice fraction;
• recombining said first juice fraction and said second juice fraction in order to produce a third juice fraction;
• combining said third juice fraction with a main supply of lime in a main liming chamber in order to degrade remaining amounts of said dissolved non-sugar impurities which are present within said third juice fraction;
• combining said third juice fraction with a secondary supply of carbon dioxide gas in a secondary carbonation chamber in order to remove said main supply of lime therefrom, said combining of said third juice fraction with said secondary supply of carbon dioxide gas producing a calcium carbonate sludge product within said third juice fraction, said calcium carbonate sludge product adsorbing residual amounts of said dissolved non-sugar impurities which are present within said third juice fraction, said secondary carbonation chamber being maintained separately from said primary carbonation chamber;
• removing said calcium carbonate sludge product from said third juice fraction in order to produce a treated juice product;
• dividing said calcium carbonate sludge product into a calcium carbonate-containing first sludge portion and a calcium carbonate-containing second sludge portion;
• routing said first sludge portion into said preliming chamber for use as said preliminary supply of calcium carbonate in treating additional quantities of beet juice materials which enter said preliming chamber;
• heating said second sludge portion to a temperature of about 980.degree.-1200.degree. C. to convert said second sludge portion into a supply of regenerated lime and a gaseous reaction product comprising carbon dioxide therein;
• dividing said supply of regenerated lime into a first lime fraction and a second lime fraction;
• routing said first lime fraction into said main liming chamber for use as said main supply of lime in treating additional quantities of beet juice materials which enter said main liming chamber;
• routing said second lime fraction into said preliming chamber for use as said preliminary supply of lime in treating additional quantities of beet juice materials which enter said preliming chamber;
• and
• routing said gaseous reaction product into at least one of said primary carbonation chamber and said secondary carbonation chamber for use therein.

A method for treating and purifying beet juice using recycled lime and recycled calcium carbonate compositions comprising the steps of:

• providing a supply of beet juice comprising water, sugar, and dissolved non-sugar impurities therein;
• heating said beet juice to a temperature of about 65.degree.-85.degree. C.;
• combining said beet juice with a preliminary supply of lime and a preliminary supply of calcium carbonate in a preliming chamber in order to produce a first juice fraction and a second juice fraction, said second juice fraction comprising a plurality of solid floc particles therein, said floc particles being formed from said non-sugar impurities in said beet juice when said preliminary supply of lime and said preliminary supply of calcium carbonate are combined with said beet juice, said preliminary supply of lime being combined with said beet juice in an amount sufficient to cause said beet juice to have a pH level above about 11.6;
• separating said first juice fraction from said second juice fraction;
• combining said second juice fraction with a primary supply of carbon dioxide gas in a primary carbonation chamber in order to remove said preliminary supply of lime from said second juice fraction, said combining of said second juice fraction and said primary supply of carbon dioxide gas producing a calcium carbonate reaction product in said second juice fraction, said calcium carbonate reaction product encapsulating said solid floc particles within said second juice fraction;
• removing said calcium carbonate reaction product and said floc particles encapsulated by said calcium carbonate reaction product from said second juice fraction;
• recombining said first juice fraction and said second juice fraction in order to produce a third juice fraction;
• heating said third juice fraction to a temperature of about 85.degree.-90.degree. C.;
• combining said third juice fraction with a main supply of lime in a main liming chamber in order to degrade remaining amounts of said dissolved non-sugar impurities which are present within said third juice fraction, said main supply of lime being combined with said third juice fraction in an amount sufficient to cause said third juice fraction to have a pH level above about 12.6;
• combining said third juice fraction with a secondary supply of carbon dioxide gas in a secondary carbonation chamber in order to remove said main supply of lime therefrom, said combining of said third juice fraction with said secondary supply of carbon dioxide gas producing a calcium carbonate sludge product within third juice fraction, said calcium carbonate sludge product adsorbing residual amounts of said dissolved non-sugar impurities which are present within said third juice fraction, said secondary carbonation chamber being maintained separately from said primary carbonation chamber;
• removing said calcium carbonate sludge product from said third juice fraction in order to produce a treated juice product;
• dividing said calcium carbonate sludge product into a calcium carbonate-containing first sludge portion and a calcium carbonate-containing second sludge portion, said dividing of said calcium carbonate sludge product comprising removing about 5-30% by weight of said calcium carbonate sludge product as said first sludge portion, and removing about 70-95% by weight of said calcium carbonate sludge product as said second sludge portion;
• routing said first sludge portion into said preliming chamber for use as said preliminary supply of calcium carbonate in treating additional quantities of beet juice materials which enter said preliming chamber;
• heating said second sludge portion to a temperature of about 980.degree.-1200.degree. C. in order to convert said second sludge portion into a supply of regenerated lime and a gaseous reaction product comprising carbon dioxide therein;
• adding a supply of extra lime to said supply of regenerated lime;
• dividing said supply of regenerated lime into a first lime fraction and a second lime fraction, said dividing of said supply of regenerated lime comprising removing about 80-85% by weight of said supply of regenerated lime as said first lime fraction, and removing about 15-20% by weight of said supply of regenerated lime as said second lime fraction;
• routing said first lime fraction into said main liming chamber for use as said main supply of lime in treating additional quantities of beet juice materials which enter said main liming chamber;
• routing said second lime fraction into said preliming chamber for use as said preliminary supply of lime in treating additional quantities of beet juice materials which enter said preliming chamber;
• and
• routing said gaseous reaction product into at least one of said primary carbonation chamber and said secondary carbonation chamber for use therein.