Beverage to Coca Cola F42/F55 Fructose Production Machinery

Product Name: Beverage to Coca Cola F42/F55 Fructose Production Machinery Model NO.: 10MT/D 30MT/D 50MT/D 100MT/D 200MT/D Customized: Customized Condition: New Press Series: Second Press Materials: Corn Appearance: Horizontal Voltage: 380V Application: Fructose Type: Fructose Trademark: YHT Transport Package: Container Specification: Customized Origin: Shijiazhuang, Hebei, China HS Code: 8438800000 Product Description F42/F55 {0><}0{>Fructose SyrupProduction LineProcess1.1.Preparation for {0><}0{>starch milk: Refinedstarchfromplantstarch was dissolvedintothewatertankto be adjusted to 19 to 20Be, then adding Na2CO3 to adjust the PH to 5.4to6.0, and addingαamylase to be ready for liquefaction.1.2{0><}0{>Liquefaction<0}:{0>,,,110oC,30,0.2MPa,,98oC,20,,.<}0{>Put the starch milk prepared to the 1st injector and inject steam directly to the starch milk. Make the temperature rise to 110ºCquickly. After entering the 1st flash evaporator, lower the temperature to 98ºCand keep it for a certaintime. The material, after initial hydrolysis, is with a lower viscidity. <0}{0>,135oC,10,95oC,2/3α-,90~120,DE12~18.<}0{>The material is then put into the 2nd injector by the pump, its temperature reaching 135ºCquickly, then it gets to the 2nd flash evaporator. The temperature in the 2nd flash evaporator declines to 95ºC. The DE volume of the material would be between 15 and 20 after its staying in the tubular reactor for 90to120 minutes.1.3. Saccharification<0}: Puthydrochloric acidinto the material after liquefaction and make the PH volume to 4.0 to4.5, while lowering the temperature from 90ºCto 60ºC. Add fungal enzymes and glucoamylaseinto it and keep stirring at that temperature. DE valuewill be 40 to60after the saccharificationperiod will take 16 to24 hours.1.4. Refining<0}:After refining, impurities, protein, fat, pigment, and edible salt are removed from the saccharification liquid. The material should now first be put into the Board frame filter. The best temperature for filtration is 70ºCto 85ºC. The insoluble protein and fat is separated and the clear and slightly colored saccharification liquid comes into being. The next section is charcoal absorptionwhich further separates the insoluble protein and pigment. Keep adding inactive carbon at the temperature between 75ºCand 85ºCin order to make the material have enough contact with active carbon. Then put the material into filter to separate carbon from it. Another round of check and filtration is needed to make sure there is no more carbon.1.5. {0><}0{>Ion exchange<0}:After filtration, amino acid and Inorganic salts are separated from the saccharification liquid. The temperature of the material should be lowered to 48 to50ºCto take ion exchange, firstly cation exchange column resin, and secondly anion-exchange column resin. During cation exchange column, Na, Fe, Ca, Cu and a part of amino acid are separated, and during anion-exchange column, chloride, sulfate, phosphate, and most of the soluble amino acid can be taken off, which makes the refined saccharification liquid come into being.1.6.Pre-concentration: After purificationDS of liquid sugar isabout 30%, the liquid sugar is into thefalling filmevaporatorto concentrate after adjusting the PHvalue, the concentration of concentratedsugaris 45to50%.1.7.Add in NaCO3 solution and dispatch pH to 7.5to7.8. pack the Isomerization of enzyme in Vertical thermal reaction tower, Glucose syrup is fed from the pillars, with flowing through the enzyme column and isomerization reaction, at last discharge from the bottom of the column, continuous operation. Mixed sugar liquid is fed the heterogeneous column with immobilized isomerase, 42% of the amount of glucose is different form a sugar called fructose, get the F- 42 fructose syrup.1.8.F42 fructose syrup decolorization:F42 fruit glucose slurry is get rid of impurity, protein, fat, pigment and edible salt after refining section. Get rid of pigment with activated carbon adsorption, add activated carbon continuously when the solution reaches 75 ºC, make material get good contact with activated carbon, Get rid of carbon with filter after reaction, checked the filter again in order to ensure that the material does not contain carbon. The best temperature for Filtering is 70to85 ºC.1.9. F42 fructose syrup ion exchange:After filtering the fruit glucose slurry further refined to amino acids and inorganic salt, the material temperature dropped to 48~50 ºCfor ion exchange, the material temperature drop to 48to50 ºCin ion exchange, the order is first cationic exchange resin, and then anion exchange resin. When the cation exchange, Sodium, calcium and iron, copper and other ingredients, and part of amino acids is off; When the anion exchange, Chloride, sulfate, phosphate and most soluble amino acids is off. The result is refined saccharification liquid.1.10. F42 Fructose syrup concentration:F42fructose syrupDSafter being refined is between45to50%,adjust the pH valueis sent to thefalling film evaporatorpre concentrationto the concentrationof about 60%,A part is feeding for the SSMB chromatographic separation, The other part is F55 mixing ingredients.1.11.SSMB chromatographic separation:The SSMB chromatographic separation system was with reference to the principle of moving bed, But the resin does not move, it Works with several resin column in series,The Material and washing water flow into respectively from different columns. The sugar liquid and liquid waste will be displaced separately from the column between them after separating. It works with countercurrent and continuous operation mode, passes through the material inlet and outletposition of adsorption equipment which belongs to the moving bed.Then have an effect which looks like that the adsorbent moves downwardcontinuously,while thematerial moves upward continuously.After the separationof operation of SSMB,fructose contentof the resulting productcan be as high as 90%.1.12.F55 fructose syrup mix preparation and refined:MixtheF90fruit syrupandthe F42fructose syrupFrom bypass together.You can get F55 fruit Portugal syrup.The mixedsyrupwill be sent to theF55 concentration process after being refined,sterilization and deodorization.1.13. F55 fructose syrupconcentration:Send the F55 fructose syrup Afterrefining into three effect falling-film evaporator for enrichment, condense itto DS77%,then we can get the F55 fruit Portugal syrup.