Dispositivo de fabricação de frutose automática industrial personalizada

Fructose Project Introduction

Starch milk adjustment: A proper DS value (DS=28%-32%), PH value, and temperature adjustment for starch milk. Starch milk can also be made by combining dry starch and water. After correction, it is then moved on to the following stage for more processing.

Liquefaction: In a jet cooker, liquefaction takes place. Ejection is utilized twice to get better results with liquefaction. After the chemical has liquefied, it is cooled in a flash tank before going to the saccharification phase.

Saccharification: The desired DE value is obtained through saccharification. The enzyme facilitates the reaction's execution. Liquefied syrup reaches the appropriate DE value after maintaining a certain amount of time. After that, a flash tank is used to chill the glucose. The following step involves further contaminants removal after chilling the glucose.

Filtration and decolorization: Protein and other contaminants in the generated glucose must be removed. Before proceeding to the following procedure, it is also necessary to remove any colored ion pigments. Protein and other contaminants are eliminated during filtering. After that, the activated carbon is utilized to remove color. The activated carbon will then be filtered out after that. The glucose is then processed further in the next processes.

Continuous ion exchange: Based on their chemical attraction behavior, the ion exchange system needs to eliminate some mixed ion contaminants that are still present in the filtered glucose. Resin is placed inside the ion exchange device. The ratio of cation to anion in the resin is 2:1. Based on their respective principles, cation and anion both attract the mixed ion. The glucose attains a high level of purity in this manner. The glucose then moves on to the following phase.

Evaporation: The desired DS value must be reached for the glucose. The glucose is concentrated through evaporation to get the desired DE level. The glucose with the proper DE is then transferred to the following area.

Isomerization: The isomerization mechanism receives glucose with the proper DS and PH values. The interior structure is then altered by glucose, becoming 42% fructose. When glucose is subjected to isomerization, fructose is converted at a rate of 42%. Fructose 42% then moves on to the following step.

Decolorization/filtration: The decolorization method must first filter the 42% fructose before using it. The decolorization procedure makes use of activated carbon. The filter then removes the activated carbon. The 42% filtered fructose then moves on to the following step.

Continuous ion exchange: Using the chemical attraction principle, ion exchange systems eliminate mixed ion contaminants. An anion and cation-containing resin is used in the ion exchange system. The fructose attains a high grade of 42% following the ion exchange procedure.

Evaporation: To achieve the specified DS value, 42% fructose is required. The fructose 42% is concentrated by evaporation to get the necessary DS value. Then, the material moves on to the following phase.

Chromatography separation and 55% fructose mixing: To create the 55% fructose, high purity fructose was combined with 42%. The 42% glucose and 55% fructose were separated using chromatography to produce the fructose. The 55% fructose is processed further at the next stage after chromatography separation.

Decolorization/filtration: Filtration removes contaminants from 55% fructose. The decolorization procedure then employs activated carbon. The filter will eliminate the activated carbon after decolorization. At processing time, the decolorization mechanism maintains the proper temperature. Then, the 55% fructose is moved on to the following step.

Mixed bed ion exchange: Mixed impurity ions are present in the 55% fructose. The contaminants are eliminated using the Mixed bed ion exchange system, and 55% fructose obtains a high purity level.

Evaporation: The refined 55% fructose is concentrated through evaporation to provide the appropriate DS value. The ideal DS value product will be produced after evaporation.