CN102524632A - Dining table sugar containing xylooligosaccharide and sucralose, and preparation method thereof - Google Patents
Dining table sugar containing xylooligosaccharide and sucralose, and preparation method thereof Download PDFInfo
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- CN102524632A CN102524632A CN2010105920952A CN201010592095A CN102524632A CN 102524632 A CN102524632 A CN 102524632A CN 2010105920952 A CN2010105920952 A CN 2010105920952A CN 201010592095 A CN201010592095 A CN 201010592095A CN 102524632 A CN102524632 A CN 102524632A
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Abstract
The present invention relates to a dining table sugar containing xylooligosaccharide and sucralose, and a preparation method thereof. The components of the dining table sugar comprise 75-93% of glucose monohydrate, 3-10% of xylooligosaccharide, 5-10% of maltodextrin, and 0.8-1.70% of sucralose. The preparation process comprises that: the maltodextrin and the sucrose are respectively added to heating containers; deionized water are respectively added to the containers, and treatments of mixing, and heating dissolving are performed; active carbon are respectively added to the resulting solutions, a filtration treatment is performed while hot, and the filtrates are respectively collected in a storage tank; the crushed glucose monohydrate and the xylooligosaccharide are mixed, the positive pressure is applied, and the resulting mixture enters a spraying fluidized bed from the bottom of the spraying fluidized bed, and acceleratively flows from bottom to top; the negative pressure is applied on the upper part of the spraying fluidized bed, and the spraying fluidized bed vibrates from top to bottom, such that the material in the spraying fluidized bed boils upwards and downwards; the refined sucralose solution is continuously sprayed and dispersed on fine sugar alcohol bodies by a multi-point spray gun on the side part of the spraying fluidized bed; the maltodextrin solution is introduced by pumping, and a continuous spray drying treatment is performed to obtain the low sugar and low calorie dining table sugar. According to the present invention, the preparation process is convenient and is easy to operate, and the sugariness of the dining table sugar of the present invention is 5-10 times the sugariness of the common sucrose.
Description
Technical field
The present invention relates to a kind of edible sweet taste material, relate in particular to a kind of fluffy granular low-calorie dining-table sugar (sweet taste material) and preparation method thereof.
Background technology
The increase of Along with people's because of too much bringing disease with sugar, people's demand safety, healthy low-sugar-content and low-calorie type dining table sugar (sweet taste material); In production procedure, reach the advanced preparation technology who puts into finished product one step completion from raw material; It is learnt from other's strong points to offset one's weaknesses, has complementary advantages to make between the sugar alcohol sweet taste on the formula for a product; Can play during product uses and cover the effect that promotes mouthfeel with synergy; People thirst for having health care again satisfying under the low prerequisite of sugariness height, heat, and occupation modeization, with cane-sugar taste safety and Health low-sugar low-calorie dining-table sugar (sweet taste material) roughly the same.
Summary of the invention
The objective of the invention is to overcome the deficiency that prior art exists, a kind of dining table sugar with xylo-oligosaccharide and Sucralose and preparation method thereof is provided, adopt the scientific technology of easy operation control, the molten speed property of product, mouthfeel, sugariness all are higher than the prior art optimum value.
The object of the invention is realized through following technical scheme:
A kind of dining table sugar with xylo-oligosaccharide and Sucralose, characteristics are to comprise following composition (percentage by weight): Dextrose Monohydrate 75～83%, xylo-oligosaccharide 3～10%, maltodextrin 5～10%, Sucralose 0.8～1.70%.
Further, above-mentioned a kind of dining table sugar with xylo-oligosaccharide and Sucralose, wherein, Dextrose Monohydrate 85%, xylo-oligosaccharide 5%, maltodextrin 8.83%, Sucralose 1.17%.
Further, above-mentioned fluffy granular low-calorie dining-table sugar (sweet taste material), said maltodextrin DE value is 10～20.
The present invention is a kind of with the sugared preparation method of the dining table of xylo-oligosaccharide and Sucralose, comprises following processing step:
1. maltodextrin, Sucralose are joined respectively in the heating container, add deionized water respectively and mix;
2. be warming up to 52～80 ℃ of dissolvings respectively, and stir;
3. add active carbon respectively in above-mentioned maltodextrin solution and the sucralose solution, be incubated 25～30 minutes, filter while hot, filtrating is pooled to respectively in the storage tank of heat tracing;
4. Dextrose Monohydrate pulverizing back and xylo-oligosaccharide are put in the spray-fluidized bed apparatus together; The mixed material of Dextrose Monohydrate, xylo-oligosaccharide also quickens to flow from the bottom entering fluidized bed with spraying of fluidized bed with spraying with malleation from bottom to top; The top of fluidized bed with spraying impose negative pressure vibrate from top to bottom make material in fluid bed up and down the boiling; The multiple spot spray gun of fluid bed sidepiece is sprayed the above-mentioned sucralose solution that refines continuously earlier and is distributed on the fine sugar alcohol body; Pump into the above-mentioned maltodextrin solution that refines again, spray-drying obtains fluffy granular low-calorie dining-table sugar (sweet taste material) continuously.
Again further, the preparation method of above-mentioned a kind of dining table sugar with xylo-oligosaccharide and Sucralose joins maltodextrin, Sucralose respectively in the heating container, adds deionized water respectively and mixes; Be warming up to 60～80 ℃ of dissolvings respectively, and stir; Add active carbon respectively, be incubated 30 minutes, filter while hot, filtrating is pooled to respectively in the storage tank that has heat tracing; Dextrose Monohydrate reaches behind 120～180 orders and xylo-oligosaccharide through pulverizing; Be sent to together in the spray-fluidized bed apparatus; The mixed material of Dextrose Monohydrate and xylo-oligosaccharide also quickens to flow from the bottom entering fluidized bed with spraying of fluidized bed with spraying with malleation from bottom to top; The top of fluidized bed with spraying imposes negative pressure and vibrates from top to bottom and make material boiling up and down in fluid bed, and control fluidized-bed layer temperature is at 35～80 ℃, and the multiple spot spray gun of fluid bed sidepiece earlier will the above-mentioned sucralose solution that refines be sprayed continuously and is distributed on the fine sugar alcohol body; After the mixing of sugar alcohol fluidisation loses surperficial moisture content; Pump into the above-mentioned maltodextrin solution that refines again, spray drying granulation obtains fluffy granular low-calorie dining-table sugar (sweet taste material) continuously.
Again further; Above-mentioned is a kind of with the sugared preparation method of the dining table of xylo-oligosaccharide and Sucralose; The bed temperature scope of said fluidized bed with spraying is 35～80 ℃; Wherein the bed temperature of phase I Sucralose spraying dispersion is 35～50 ℃, and the bed temperature of second stage maltodextrin mist projection granulating is 50～80 ℃.
Again further, above-mentioned is a kind of with the sugared preparation method of the dining table of xylo-oligosaccharide and Sucralose, and in the phase I of said Spray Mixing fluid bed, the Sucralose spraying is dispersed in fluidisation and smashes on the fine sugar alcohol crystal body; In second stage, the maltodextrin spray drying granulation is on the noncrystal of mixing sugar alcohol.
Substantive distinguishing features and obvious improvement that technical scheme of the present invention is outstanding are mainly reflected in:
Adopt the negative pressure fluid bed fluidization technique of scientific formula, uses advanced to combine the multi-point atomizing method, time sharing segment control appliance bed temperature efficiently solves even dispersion, coats problems such as granulation, drying.With Dextrose Monohydrate, xylo-oligosaccharide, maltodextrin, Sucralose is primary raw material; Modify uniformly and coat through preparation method to sugariness, make product sweetness reach 5～10 times of common sucrose, products obtained therefrom does not have smell, does not have color; Soluble in water; Easy to use when these fluffy granular low-calorie dining-table sugar (sweet taste material) people are edible, its preparation process science is simple and easy to operate, is fit to very much large-scale production.
Description of drawings
Below in conjunction with accompanying drawing technical scheme of the present invention is described further:
Fig. 1: process chart of the present invention.
The specific embodiment
A kind of dining table sugar with xylo-oligosaccharide and Sucralose of the present invention, its composition is: Dextrose Monohydrate 75～83%, xylo-oligosaccharide 3～10%, maltodextrin 5～10%, Sucralose 0.8～1.70%.Ideal formulations is: Dextrose Monohydrate 85%, xylo-oligosaccharide 5%, maltodextrin 8.83%, Sucralose 1.17%.
As shown in Figure 1, a kind of with the sugared preparation technology of the dining table of xylo-oligosaccharide and Sucralose: as at first, maltodextrin, Sucralose to be joined respectively in the heating container, add deionized water respectively and mix; Be warming up to 52～80 ℃ of dissolvings respectively, and stir; Add active carbon in above-mentioned maltodextrin solution and the sucralose solution respectively, be incubated 25～30 minutes, filter while hot, filtrating is pooled to respectively in the storage tank of heat tracing; Then; Dextrose Monohydrate is pulverized back and xylo-oligosaccharide to be put in the spray-fluidized bed apparatus (at heating temperature control and technological with the boiling that in fluid bed, circulates of sugar alcohol material through the positive negative pressure boiling of equipment; Mix that fluidisation is anhydrated and fluffy processing; Sugar alcohol mixtures material → malleation material quickens to flow from bottom to top → and negative pressure vibrates → makes material boiling up and down in fluid bed → by the fluid bed side multiple spot spray gun liquid material ejection fog-like liquid of naming a person for a particular job from top to bottom; Be sprayed onto on the trickle solid material body of boiling); The mixed material of Dextrose Monohydrate and xylo-oligosaccharide also quickens to flow from the bottom entering fluidized bed with spraying of fluidized bed with spraying with malleation from bottom to top; The top of fluidized bed with spraying impose negative pressure vibrate from top to bottom make material in fluid bed up and down the boiling; The multiple spot spray gun of fluid bed sidepiece is sprayed the above-mentioned sucralose solution that refines continuously earlier and is distributed on the fine sugar alcohol body, and the bed temperature that the spraying of control Sucralose disperses is 35～50 ℃, and the Sucralose even spraying is dispersed on the mixing sugar alcohol crystalline solid of powder; The rising bed temperature; At mixing sugar alcohol after fluidisation loses surface crystallization water; Pump into the above-mentioned maltodextrin solution that refines again; Continuous spray drying granulation, the bed temperature of maltodextrin mist projection granulating controlled well is 50～80 ℃, the maltodextrin spray drying granulation is on the noncrystalline fluffy body of sugar alcohol; Obtain even sugariness and modify fluffy good shape product.
Embodiment 1:
9 kilograms of maltodextrins and deionized water are dissolved in a stainless steel reacting by heating pot for 20 kilograms; 0.83 kilogram of Sucralose and deionized water are also dissolved in another stainless steel reacting by heating pot for 15 kilograms, and material is heated to 62 ℃ by chuck in the pot, starts stirring; Add 1 kilogram of active carbon respectively; Be incubated 30 minutes, filter while hot, for use in the storage tank that collects in the chuck insulation respectively of filtrating; 85 kilograms of Dextrose Monohydrates, 5.17 kilograms of xylo-oligosaccharides, pulverizing reaches 130 orders through pulverizer; Be sent in the spray-fluidized bed apparatus, the mixed material of Dextrose Monohydrate and xylo-oligosaccharide gets into the fluidized bed with spraying from the bottom of fluidized bed with spraying and quickens from bottom to top with malleation and flows, and the top of fluidized bed with spraying imposes negative pressure and vibrates from top to bottom and make material boiling up and down in fluid bed; The multiple spot spray gun of fluid bed sidepiece is sprayed the above-mentioned sucralose solution that refines continuously earlier and is distributed on the fine sugar alcohol body; Control fluidized-bed layer temperature is 35～50 ℃, and the multiple spot even spraying is disperseed, after operation is accomplished; Improve bed temperature to 50～80 ℃ again; After Dextrose Monohydrate, the mixing of xylo-oligosaccharide fluidisation lose surface crystallization water, pump into the above-mentioned maltodextrin solution that refines, continuously spray drying granulation; Control air quantity and mist flow well, obtain even sugariness and modify good fluffy granular product.
Embodiment 2:
8.83 kilograms of maltodextrins and deionized water are dissolved in a stainless steel reacting by heating pot for 25 kilograms; 1.17 kilograms of Sucraloses and deionized water are also dissolved in another stainless steel reaction pot for 15 kilograms, and material is heated to 52 ℃ by chuck in the pot, starts stirring; Add 2 kilograms of active carbons respectively; Be incubated 30 minutes, filter while hot, for use in the storage tank that collects in the chuck insulation respectively of filtrating; 85 kilograms of Dextrose Monohydrates, 5 kilograms of xylo-oligosaccharides reach 150 orders through pulverizing; Be sent to together and carry out fluidisation in the spray-fluidized bed apparatus and mix, the mixed material of Dextrose Monohydrate and xylo-oligosaccharide gets into the fluidized bed with spraying and quickens from bottom to top from the bottom of fluidized bed with spraying with malleation and flows, and the top of fluidized bed with spraying imposes negative pressure and vibrates from top to bottom material is seethed with excitement up and down in fluid bed; The multiple spot spray gun of fluid bed sidepiece is sprayed the above-mentioned sucralose solution that refines continuously earlier and is distributed on the fine sugar alcohol body; 35～40 ℃ of control fluidized-bed layer temperature, even spraying is disperseed, after operation is accomplished; Improve bed temperature to 50～80 ℃ again; After making Dextrose Monohydrate, the mixing of xylo-oligosaccharide fluidisation lose surface crystallization water, pumping into the above-mentioned maltodextrin solution that refines, continuously spray granulating and drying; Control air quantity and mist flow well, obtain even sugariness and modify good fluffy granular product.
Embodiment 3:
4 kilograms of maltodextrins and deionized water are dissolved in a stainless steel reacting by heating pot for 25 kilograms; 1 kilogram of Sucralose and deionized water are also dissolved in another stainless steel reacting by heating pot for 15 kilograms, and material is heated to 60 ℃ by chuck in the pot, starts stirring; Add 2.0 kilograms of active carbons respectively; Be incubated 30 minutes, filter while hot, for use in the storage tank that collects in the chuck insulation respectively of filtrating; 88 kilograms of Dextrose Monohydrates, 4 kilograms of xylo-oligosaccharides, pulverizing reaches 160 orders through pulverizer; Be sent to together in the spray-fluidized bed apparatus, the mixed material of Dextrose Monohydrate and xylo-oligosaccharide gets into the fluidized bed with spraying from the bottom of fluidized bed with spraying and quickens from bottom to top with malleation and flows, and the top of fluidized bed with spraying imposes negative pressure and vibrates from top to bottom and make material boiling up and down in fluid bed; The multiple spot spray gun of fluid bed sidepiece is sprayed the above-mentioned sucralose solution that refines continuously earlier and is distributed on the fine sugar alcohol body; Control 35～42 ℃ of fluidized-bed layer temperature well, the multiple spot even spraying is disperseed, after operation is accomplished; Improve bed temperature to 50～80 ℃ again; After Dextrose Monohydrate, the mixing of xylo-oligosaccharide fluidisation lose surface crystallization water, pump into the above-mentioned maltodextrin solution that refines, continuously spray drying granulation; Control air quantity and mist flow well, obtain even sugariness and modify good fluffy granular product.
Embodiment 4:
10 kilograms of maltodextrins and deionized water are dissolved in a stainless steel reacting by heating pot for 30 kilograms; 12 kilograms also another dissolves in stainless steel reacting by heating pot with deionized water with 1.17 kilograms of Sucraloses, and material is heated to 80 ℃ by chuck in the pot, starts stirring; Add 3.0 kilograms of active carbons respectively; Be incubated 35 minutes, filter while hot, for use in the storage tank that collects in the chuck insulation respectively of filtrating; 82 kilograms of Dextrose Monohydrates, 6.83 kilograms of xylo-oligosaccharides, pulverizing reaches 180 orders through pulverizer; Be sent to fluidisation in the spray-fluidized bed apparatus together, the mixed material of Dextrose Monohydrate and xylo-oligosaccharide gets into the fluidized bed with spraying from the bottom of fluidized bed with spraying and quickens from bottom to top with malleation and flows, and the top of fluidized bed with spraying imposes negative pressure and vibrates from top to bottom and make material boiling up and down in fluid bed; The multiple spot spray gun of fluid bed sidepiece is sprayed the above-mentioned sucralose solution that refines continuously earlier and is distributed on the fine sugar alcohol body; Control 35～50 ℃ of fluidized-bed layer temperature well, the multiple spot even spraying is disperseed, after operation is accomplished; Improve bed temperature to 50～80 ℃ again; After Dextrose Monohydrate, xylo-oligosaccharide fluidisation lose surface crystallization water, pumping into the above-mentioned maltodextrin solution that refines, continuously the Spray Mixing drying-granulating; Control air quantity and mist flow well, obtain the good fluffy granular product of even sugariness decorations.
Embodiment 5:
6.65 kilograms of maltodextrins and deionized water are dissolved in a stainless steel reacting by heating pot for 22 kilograms; 1.34 kilograms of Sucraloses and deionized water are also dissolved in another stainless steel reacting by heating pot for 20 kilograms, and material is heated to 62 ℃ by chuck in the pot, starts stirring; Add 1.5 kilograms of active carbons respectively; Be incubated 30 minutes, filter while hot, for use in the storage tank that collects in the chuck insulation respectively of filtrating; 86 kilograms of Dextrose Monohydrates, 6 kilograms of xylo-oligosaccharides, pulverizing reaches 130 orders through pulverizer; Be sent in the spray-fluidized bed apparatus, the mixed material of Dextrose Monohydrate and xylo-oligosaccharide gets into the fluidized bed with spraying from the bottom of fluidized bed with spraying and quickens from bottom to top with malleation and flows, and the top of fluidized bed with spraying imposes negative pressure and vibrates from top to bottom and make material boiling up and down in fluid bed; The multiple spot spray gun of fluid bed sidepiece is sprayed the above-mentioned sucralose solution that refines continuously earlier and is distributed on the fine sugar alcohol body; Control fluidized-bed layer temperature is 35～50 ℃, and the multiple spot even spraying is disperseed, after operation is accomplished; Improve bed temperature to 50～80 ℃ again; After Dextrose Monohydrate, the mixing of xylo-oligosaccharide fluidisation lose surface crystallization water, pump into the above-mentioned maltodextrin solution that refines, continuously spray drying granulation; Control air quantity and mist flow well, obtain even sugariness and modify good fluffy granular product.
Embodiment 6:
10 kilograms of maltodextrins and deionized water are dissolved in a stainless steel reacting by heating pot for 30 kilograms; 1.66 kilograms of Sucraloses and deionized water are also dissolved in another stainless steel reaction pot for 10 kilograms, and material is heated to 52 ℃ by chuck in the pot, starts stirring; Add 2 kilograms of active carbons respectively; Be incubated 30 minutes, filter while hot, for use in the storage tank that collects in the chuck insulation respectively of filtrating; 83 kilograms of Dextrose Monohydrates, 5.34 kilograms of xylo-oligosaccharides reach 150 orders through pulverizing; Be sent to together and carry out fluidisation in the spray-fluidized bed apparatus and mix, the mixed material of Dextrose Monohydrate and xylo-oligosaccharide gets into fluidized bed with spraying with malleation from the bottom of fluidized bed with spraying bottom gets into the fluidized bed with spraying and quickens from bottom to top flows, and the top of fluidized bed with spraying imposes negative pressure and vibrates from top to bottom material is seethed with excitement up and down in fluid bed; The multiple spot spray gun of fluid bed sidepiece is sprayed the above-mentioned sucralose solution that refines continuously earlier and is distributed on the fine sugar alcohol body; Control fluidized-bed layer temperature is 35～50 ℃, and the multiple spot even spraying is disperseed, after operation is accomplished; Improve bed temperature to 50～80 ℃ again; After Dextrose Monohydrate, the mixing of xylo-oligosaccharide fluidisation lose surface crystallization water, pump into the above-mentioned maltodextrin solution that refines, continuously spray drying granulation; Control air quantity and mist flow well, obtain even sugariness and modify good fluffy granular product.
Through detecting, the multiple low-calorie dining-table sugar of fluffy granular (sweet taste material) that adopts technical scheme of the present invention to obtain, its main performance index is seen table 1.
Table 1
| Test item | Embodiment 1 | Embodiment 2 | Embodiment 3 | Embodiment 4 |
| Particle size | 30～60 orders | 30～60 orders | 30～60 orders | 30～60 orders |
| Sugariness (sucrose contrast) | 5 times | 7 times | 6 times | 7 times |
| Outward appearance | White particle | White particle | White particle | White particle |
| Bulk density (g/mm 3) | 0.60 | 0.62 | 0.63 | 0.66 |
| Test item | Embodiment 5 | Embodiment 6 | ||
| Particle size | 30～60 orders | 30～60 orders | ||
| Sugariness (sucrose contrast) | 8 times | 10 times | ||
| Outward appearance | White particle | White particle | ||
| Bulk density (g/mm3) | 0.60 | 0.62 |
The stability test of dining table sugar (sweet taste material) is to check the sweet taste material to guarantee the ability that undergoes no deterioration within a certain period of time, and the dining table sugar product of the embodiment of the invention was stored 3 years at normal temperatures, phenomenons such as rotten and sugariness reduction occur, and the stability ten minutes is superior.
Sugariness, the proportion degree of modification of fluffy granular low-calorie dining-table of the present invention sugar (sweet taste material) will be according to the adjustment of Sucralose in consumption, select the common sucrose sugariness usually for use 5～10 times; The use needs that relatively are fit to people; Form according to prescription, under same sugariness situation, people only are 1/6～1/12 of common sucrose to the absorption of heat; Low-sugar low-calorie dining-table sugar is the sweet taste article of low-calorie, and this dining table sugar satisfies pursues healthy needs of people.
What need understand is: the above only is a preferred implementation of the present invention; For those skilled in the art; Under the prerequisite that does not break away from the principle of the invention, can also make some improvement and retouching, these improvement and retouching also should be regarded as protection scope of the present invention.
Claims (5)
1. the dining table sugar with xylo-oligosaccharide and Sucralose is characterized in that comprising following composition (percentage by weight): Dextrose Monohydrate 75～93%, xylo-oligosaccharide 3～10%, maltodextrin 5～10%, Sucralose 0.8～1.70%.
2. a kind of dining table sugar with xylo-oligosaccharide and Sucralose according to claim 1 is characterized in that its component has following percentage by weight: Dextrose Monohydrate 85%, xylo-oligosaccharide 5%, maltodextrin 8.83%, Sucralose 1.17%.
3. a kind of dining table sugar with xylo-oligosaccharide and Sucralose according to claim 1 and 2, it is characterized in that: said maltodextrin DE value is 10～20.
4. claim 1 is described a kind of with the sugared preparation method of the dining table of xylo-oligosaccharide and Sucralose, it is characterized in that: comprise following processing step---
1. maltodextrin, Sucralose are joined respectively in the heating container, add deionized water respectively and mix;
2. be warming up to 52～80 ℃ of dissolvings respectively, and stir;
3. add active carbon respectively in above-mentioned maltodextrin solution and the sucralose solution, be incubated 25～30 minutes, filter while hot, for use in the storage tank that is pooled to heat tracing respectively of filtrating;
4. Dextrose Monohydrate pulverizing back and xylo-oligosaccharide are put in the spray-fluidized bed apparatus together; The mixed material of Dextrose Monohydrate, xylo-oligosaccharide is also quickened to flow from the bottom entering fluidized bed with spraying of fluidized bed with spraying with malleation from bottom to top; The top of fluidized bed with spraying impose negative pressure vibrate from top to bottom make material in fluid bed up and down the boiling; The multiple spot spray gun of fluid bed sidepiece is sprayed the above-mentioned sucralose solution that refines continuously earlier and is distributed on the fine sugar alcohol body; Pump into the above-mentioned maltodextrin solution that refines again, spray-drying obtains fluffy granular low-calorie dining-table sugar continuously.
5. according to claim 4 a kind of with the sugared preparation method of the dining table of xylo-oligosaccharide and Sucralose, it is characterized in that: maltodextrin, Sucralose are joined respectively in the container, add deionized water respectively and mix; Be warming up to 60～80 ℃ of dissolvings respectively, and stir; Add active carbon respectively, be incubated 30 minutes, filter while hot, filtrating is pooled to respectively in the storage tank that has heat tracing; Dextrose Monohydrate reaches behind 120～180 orders and xylo-oligosaccharide through pulverizing; Be sent to together in the spray-fluidized bed apparatus; The mixed material of Dextrose Monohydrate, xylo-oligosaccharide also quickens to flow from the bottom entering fluidized bed with spraying of fluidized bed with spraying with malleation from bottom to top; The top of fluidized bed with spraying imposes negative pressure and vibrates from top to bottom and make material boiling up and down in fluid bed, and control fluidized-bed layer temperature is at 35～80 ℃, and the multiple spot spray gun of fluid bed sidepiece earlier will the above-mentioned sucralose solution that refines be sprayed continuously and is distributed on the fine sugar alcohol body; After the mixing of sugar alcohol fluidisation loses surperficial moisture content; Pump into the above-mentioned maltodextrin solution that refines again, spray drying granulation obtains fluffy granular low-calorie dining-table sugar continuously.
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| CN103039787A (en) * | 2012-12-26 | 2013-04-17 | 苏州工业园区尚融科技有限公司 | Preparation method of low-sugar low-calorie table sugar |
| CN103766697A (en) * | 2014-01-07 | 2014-05-07 | 长春禾甜科技有限责任公司 | Sugar-free sweetener and preparation method thereof |
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Application publication date: 20120704 |