8results about "Sugar crystal separation" patented technology

Systems and methods for preparing compound crystals of erythritol and high-intensity sweeteners are provided. The systems may comprise a fermentation liquid storage tank (1), a ceramic membrane filtration system (2), a nanofiltration system (3), a first evaporator (4), a first crystallization kettle (5), a first centrifuge (6), a sugar dissolution tank (7), a decolorization tank (8), an ion exchange column (9), a blending tank (10), a second evaporator (11), a second crystallization kettle (12), a second centrifuge (13), a hot-air drying tank (14), a fluidized drying bed (15), and a finished product tank (16) sequentially connected through pipelines. The systems may further comprise a high-intensity sweetener storage tank (17), a primary mother liquor tank (18), and a secondary mother liquor tank (19). The finished product tank (16) may store a prepared compound crystallization product of the erythritol and the high-intensity sweetener.

The utility model discloses a separation device for producing L-arabinose, which comprises a crystallization box, a feeding pipe is fixedly arranged at the top of the crystallization box, the top of the feeding pipe is in threaded connection with a threaded cover, a cooling pipe is fixedly arranged on the surface of the crystallization box, and a temperature sensor is fixedly arranged at the top of the crystallization box. The detection end of the temperature sensor extends into the crystallization box, a connecting assembly is fixedly installed at the bottom of the crystallization box, a filter box is arranged at the bottom of the crystallization box through the connecting assembly, a vibration assembly is arranged at the top of the filter box, a frame is slidably connected into the filter box, and a filter plate is fixedly installed on the inner wall of the frame. A limiting assembly is arranged on the front side of the filtering box, and a discharging pipe is fixedly installed at the bottom of the filtering box. The L-arabinose crystals adhered to the crystallization box can be conveniently shaken off, so that the L-arabinose crystals adhered to the crystallization box can be conveniently cleaned, and the waste of the L-arabinose crystals is avoided.

A continuous process for obtaining a crystalline monosaccharide, comprising: - a continuous crystallization of the monosaccharide in a main crystallizer (10), - wherein in the main crystallizer (10) an evaporation and / or cooling crystallization is continuously carried out on a crystal suspension in order to allow crystals of the monosaccharide to grow in the crystal suspension, - separating crystals of the monosaccharide from the crystal suspension to obtain crystalline monosaccharide; - the continuous formation of a mass of crystallization magma for the main crystallizer (10) in a cascade, - wherein the cascade comprises at least a first (13) and a last stage (15) connected in series, and each stage comprises at least one pre-crystallizer (13A, 15A), - wherein in the at least one pre-crystallizer (13A) of the first stage (13), solution containing monosaccharide is seeded by monosaccharide seed crystals to obtain a pre-crystallization magma, and a mass of crystallization magma for the downstream stage (14, 15) is formed from the pre-crystallization magma by means of cooling crystallization and / or evaporation crystallization, and - wherein a solution containing monosaccharide and a mass of crystallization magma from the preceding stage are fed into the at least one pre-crystallizer (15A, 15B, 15C) of the last stage (15) in order to obtain a pre-crystallization magma, and a mass of crystallization magma for the main crystallizer (10) is formed from the pre-crystallization magma in the at least one pre-crystallizer (15A, 15B, 15C) of the last stage (15) by means of cooling crystallization and / or evaporation crystallization; - continuously feeding a solution containing the monosaccharide and a mass of crystallization magma from the at least one pre-crystallizer (15A, 15B, 15C) of the last stage (15) of the cascade into the main crystallizer (10) to provide the crystal suspension, the method being characterized in that the mass of crystallization magma formed in a pre-crystallizer (14A, 14B, 15A, 15B, 15C) of a stage (14, 15) exceeds the mass of crystallization magma formed in a pre-crystallizer (13A, 13B, 14A, 14B, 15A, 15B, 15C) of the preceding stage (13, 14) by a factor of 2 to 12.

The invention relates to a continuous method for obtaining a crystalline monosaccharide, comprising: continuous crystallization of the monosaccharide in a main crystallizer (10), wherein crystallization by evaporation and / or crystallization by cooling is carried out continuously on a crystal suspension in the main crystallizer in order to allow crystals of the monosaccharide to grow in the crystal suspension; separation of crystals of the monosaccharide out of the crystal suspension to obtain crystalline monosaccharide; continuous formation of a mass of crystallization magma for the main crystallizer (10) in a cascade, wherein the cascade comprises at least one first stage (13) and a final stage (15) connected in series and each stage comprises at least one pre-crystallizer (13A, 15A), wherein, in the at least one pre-crystallizer (13A) of the first stage (13), a solution is seeded with monosaccharide by means of monosaccharide seed crystals in order to obtain a pre-crystallization magma, and a mass of crystallization magma for the downstream stage (14, 15) is formed from the pre-crystallization magma by means of crystallization by cooling and / or crystallization by evaporation, and wherein a solution containing monosaccharide and a mass of crystallization magma from the upstream stage is supplied to the at least one pre-crystallizer (15A, 15B, 15C) of the final stage (15) to obtain a pre-crystallization magma, and in the at least one pre-crystallizer (15A, 15B, 15C) of the final stage (15) a mass of crystallization magma for the main crystallizer (10) is formed from the pre-crystallisation magma by means of crystallization by cooling and / or crystallization by evaporation; the continuous supply of a solution containing the monosaccharide and a mass of crystallization magma from the at least one pre-crystallizer (15A, 15B, 15C) of the final stage (15) of the cascade to the main crystallizer (10) to provide the crystal suspension.

The invention discloses a method for preventing sugar particle entanglement and preventing moisture in a sulfurous acid method sugar making process, mixed juice is subjected to physical impurity removal, then the sulfurous acid method sugar making process is used for producing white granulated sugar, then corn starch is added, sugar particle entanglement can be prevented, and sugar powder can effectively prevent moisture. Comprising the following steps: sugarcane juice extraction, preliming, physical impurity removal, first concentration, activated carbon filtration, reverse osmosis membrane filtration, stoving neutralization, heating, sedimentation, second concentration, crystallization, honey separation, corn starch addition, and mixing and stirring. The sugar prepared by the method can reduce entanglement of sugar grains, improve the moisture resistance, prolong the shelf life of the product and reduce the loss in the transportation and storage process, and can be directly used as a seasoning raw material of milk tea, cakes and other products.

The invention discloses a sugar manufacturing method for improving the production efficiency of baked pastries, which is characterized in that after mixed juice is subjected to physical impurity removal, white granulated sugar is produced by using a sulfurous acid method sugar manufacturing process, and sugar after wheat flour is added is used as a basic raw material for producing the baked pastries, so that the production efficiency can be improved, and large-scale production is facilitated. Comprising the following steps: sugarcane juice extraction, preliming, physical impurity removal, primary concentration, activated carbon filtration, reverse osmosis membrane filtration, stoving neutralization, heating, sedimentation, secondary concentration, crystallization, honey separation, wheat flour addition, and mixing and stirring. The sugar prepared by the method is used as a base material for producing baked pastries, so that the production processes of cakes, biscuits and other baked pastries can be reduced, the production efficiency is improved, and great convenience is provided for large-scale production.

The present application relates to a kind of erythritol and high-fold sweetener complex crystallization preparation system and method thereof, system includes sequentially through pipeline communication's fermentation broth storage tank, ceramic membrane filtration system, nanofiltration system, first evaporator, first crystallization kettle, first centrifuge, dissolve sugar tank, decoloring tank, ion exchange column, blending tank, second evaporator, second crystallization kettle, second centrifuge, hot air drying tank, fluidized drying bed and finished product tank, also includes high-fold sweetener storage tank, primary mother liquor tank and secondary mother liquor tank, fermentation broth storage tank is equipped with the feed inlet of sterilized erythritol fermentation liquor, blending tank is equipped with the feed inlet of high-fold sweetener, first centrifuge is communicated with primary mother liquor tank, primary mother liquor tank is communicated with first evaporator, second centrifuge is communicated with secondary mother liquor tank, secondary mother liquor tank is communicated with blending tank, finished product tank stores the erythritol and high-fold sweetener complex crystallization product prepared by preparation.The complex crystallization particle size of the present application is concentrated and controllable, and the production cost is reduced.