CN101810299A - Composite sugar-free low-calorie sweetener and manufacturing method thereof - Google Patents
Composite sugar-free low-calorie sweetener and manufacturing method thereof Download PDFInfo
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- CN101810299A CN101810299A CN200910249970A CN200910249970A CN101810299A CN 101810299 A CN101810299 A CN 101810299A CN 200910249970 A CN200910249970 A CN 200910249970A CN 200910249970 A CN200910249970 A CN 200910249970A CN 101810299 A CN101810299 A CN 101810299A
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- 239000002131 composite material Substances 0.000 title claims abstract description 26
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 16
- 235000013615 non-nutritive sweetener Nutrition 0.000 title claims abstract description 11
- 238000005507 spraying Methods 0.000 claims abstract description 48
- 239000000463 material Substances 0.000 claims abstract description 38
- 229920002774 Maltodextrin Polymers 0.000 claims abstract description 35
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- 229940035034 maltodextrin Drugs 0.000 claims abstract description 32
- SPFMQWBKVUQXJV-BTVCFUMJSA-N (2r,3s,4r,5r)-2,3,4,5,6-pentahydroxyhexanal;hydrate Chemical compound O.OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C=O SPFMQWBKVUQXJV-BTVCFUMJSA-N 0.000 claims abstract description 28
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 24
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- 238000000034 method Methods 0.000 claims abstract description 17
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- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 16
- 238000010438 heat treatment Methods 0.000 claims abstract description 15
- 239000007921 spray Substances 0.000 claims abstract description 14
- 239000000706 filtrate Substances 0.000 claims abstract description 11
- 238000002156 mixing Methods 0.000 claims abstract description 11
- 238000003860 storage Methods 0.000 claims abstract description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 7
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 7
- 235000009508 confectionery Nutrition 0.000 claims description 37
- 239000012530 fluid Substances 0.000 claims description 24
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 claims description 20
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- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 abstract description 6
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- HLIAVLHNDJUHFG-HOTGVXAUSA-N neotame Chemical compound CC(C)(C)CCN[C@@H](CC(O)=O)C(=O)N[C@H](C(=O)OC)CC1=CC=CC=C1 HLIAVLHNDJUHFG-HOTGVXAUSA-N 0.000 abstract 3
- 235000019412 neotame Nutrition 0.000 abstract 3
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- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 abstract 2
- AYRXSINWFIIFAE-SCLMCMATSA-N Isomaltose Natural products OC[C@H]1O[C@H](OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C=O)[C@@H](O)[C@@H](O)[C@@H]1O AYRXSINWFIIFAE-SCLMCMATSA-N 0.000 abstract 2
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- TVXBFESIOXBWNM-UHFFFAOYSA-N Xylitol Natural products OCCC(O)C(O)C(O)CCO TVXBFESIOXBWNM-UHFFFAOYSA-N 0.000 description 1
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- HEBKCHPVOIAQTA-UHFFFAOYSA-N meso ribitol Natural products OCC(O)C(O)C(O)CO HEBKCHPVOIAQTA-UHFFFAOYSA-N 0.000 description 1
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Abstract
The invention relates to a composite sugar-free low-calorie sweetener and a manufacturing method thereof. The composite sugar-free low-calorie sweetener comprises the following ingredients by weight percent: 50-69 percent of dextrose monohydrate, 15-30 percent of sorbitol, 5-13 percent of isomaltose hypgather, 4-8 percent of maltodextrin and 0.7-4.32 percent of neotame. The technique comprises the following steps: respectively adding the maltodextrin and the neotame into a heating container, respectively adding deionized water for mixing, and rising temperature for dissolving; respectively adding active carbon into the solution, filtering with heat, and respectively collecting the filtrate into a storage tank; leading the mixed material after crushing the dextrose monohydrate, the sorbitol and the isomaltose hypgather to enter a bed from the bottom part of the spray fluidized bed by positive pressure and to flow from bottom to top in a speed-increasing manner, applying negative pressure on the upper part of the spraying fluidized bed to lead the spraying fluidized bed to vibrate from top to bottom so as to lead the material to boil from top to bottom in the bed, firstly spraying and dispersing the refined neotame solution continuously on fine sugar alcohol bodies by a multi-point spray gun of the side part of the fluidized bed, then pumping into the maltodextrin solution, continuously spraying and drying to obtain the sugar-free low-calorie sweetener. The sweetness of a product is 50-300 times of that of a common cane sugar.
Description
Technical field
The present invention relates to a kind of edible sweet taste material, relate in particular to a kind of composite sugar-free low-calorie sweetener and manufacture method thereof.
Background technology
Along with the increase of people because of too much bringing disease, people's demand safety, health, and the sweet low-sugar-content and low-calorie type sweet taste material of mouthfeel with sugar; The present invention reaches in production procedure from raw material and puts into the Advanced Manufacturing Technology that finished product one step finishes; 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 satisfying under the low prerequisite of sugariness height, heat, and occupation modeization, with cane-sugar taste roughly the same, the salubriouser safety and Health low-sugar-content and low-calorie type sweet taste material of mouthfeel.
Summary of the invention
The objective of the invention is to overcome the deficiency that prior art exists, a kind of composite low-sugar low-calorie sweetening agent and manufacture method thereof are provided, adopt the scientific technology of easy operation control, the molten speed of product, mouthfeel, local flavor, sugariness all are higher than the prior art optimum value.
Purpose of the present invention is achieved through the following technical solutions:
A kind of composite low-sugar low-calorie sweetening agent, characteristics are to comprise following composition (percentage by weight): Dextrose Monohydrate 50~69%, D-sorbite 15~30%, oligoisomaltose 5~13%, maltodextrin 4~8%, knob sweet 0.7~4.32%.
Further, above-mentioned a kind of composite sugar-free low-calorie sweetener, wherein, Dextrose Monohydrate 64.28%, D-sorbite 25%, oligoisomaltose 5%, maltodextrin 5%, knob sweet 0.72%.
The manufacture method of composite low-sugar low-calorie sweetening agent of the present invention comprises following processing step:
1. with maltodextrin, knob is sweet joins respectively in the heating container, add deionized water respectively and mix;
2. be warming up to 50~80 ℃ of dissolvings respectively, and stir;
3. add active carbon respectively in above-mentioned maltodextrin solution and the sweet solution of knob, be incubated 25~30 minutes, filter while hot, filtrate is pooled to respectively in the storage tank of heat tracing;
4. with Dextrose Monohydrate, D-sorbite and oligoisomaltose are put in the spray-fluidized bed apparatus after pulverizing, with Dextrose Monohydrate, the mixed material of D-sorbite and oligoisomaltose enters the fluidized bed with spraying with malleation from the bottom of fluidized bed with spraying and quickens from bottom to top and flows, 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 sweet solution of the above-mentioned knob 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 composite low-sugar low-calorie sweetening agent continuously.
Again further, the manufacture method of above-mentioned a kind of composite low-sugar low-calorie sweetening agent with maltodextrin, knob is sweet joins 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, filtrate is pooled to respectively in the storage tank that has heat tracing; With Dextrose Monohydrate, D-sorbite and oligoisomaltose reach 120~180 orders through pulverizing, be sent in the spray-fluidized bed apparatus, the mixed material of above-mentioned various sugar alcohols entered the fluidized bed with spraying and quicken from bottom to top from the bottom of fluidized bed with spraying with malleation flow, 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, control fluidized-bed layer temperature is at 35~80 ℃, the multiple spot spray gun of fluid bed sidepiece is sprayed the sweet solution of the above-mentioned knob that refines continuously earlier 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 composite low-sugar low-calorie sweetening agent continuously.
Again further, the manufacture method of above-mentioned a kind of composite low-sugar low-calorie sweetening agent, the bed temperature scope of described fluidized bed with spraying is 35~80 ℃, wherein the bed temperature of the sweet spraying dispersion of phase I knob is 35~50 ℃, and the bed temperature of second stage maltodextrin mist projection granulating is 50~80 ℃.
Again further, the manufacture method of above-mentioned a kind of composite low-sugar low-calorie sweetening agent, in the phase I of described spraying mixed fluidized bed, the sweet spraying of knob 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 solution of the present invention is outstanding are mainly reflected in:
With Dextrose Monohydrate, D-sorbite, oligoisomaltose, knob is sweet is primary raw material, modifies uniformly and coats by preparation method to sugariness, makes product sweetness reach 50~300 times of common sucrose, products obtained therefrom does not have smell, do not have color, and is soluble in water.The negative pressure fluid bed fluidization technique that adopts scientific formula, uses advanced is in conjunction with the multi-point atomizing method, and time sharing segment control appliance bed temperature efficiently solves even dispersion, coats problems such as granulation, drying.This fluffy granular composite low-sugar low-calorie sweetening agent is easy to use, and its process for making 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 solution of the present invention is described further:
Fig. 1: process chart of the present invention.
The specific embodiment
A kind of composite low-sugar low-calorie sweetening agent, its composition is: Dextrose Monohydrate 50~69%, D-sorbite 15~30%, oligoisomaltose 5~13%, maltodextrin 4~8%, knob sweet 0.7~4.32%.Ideal formulations is: Dextrose Monohydrate 64.28%, D-sorbite 25%, oligoisomaltose 5%, maltodextrin 5%, knob sweet 0.72%.
As shown in Figure 1, a kind of manufacturing process of composite low-sugar low-calorie sweetening agent: at first, with maltodextrin, knob is sweet joins respectively in the heating container, add deionized water respectively and mix; Be warming up to 50~80 ℃ of dissolvings respectively, and stir; Add active carbon respectively in the sweet solution of above-mentioned maltodextrin solution and knob, be incubated 25~30 minutes, filter while hot, filtrate is pooled to respectively in the storage tank of heat tracing; Then, with Dextrose Monohydrate, put into after D-sorbite and oligoisomaltose are pulverized in the spray-fluidized bed apparatus (heating temperature control and by the positive negative pressure boiling of equipment technology with the boiling that in fluid bed, circulates of sugar alcohol material, 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 above-mentioned various sugar alcohols entered the fluidized bed with spraying and quicken from bottom to top from the bottom of fluidized bed with spraying with malleation flow, 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 sweet solution of the above-mentioned knob that refines continuously earlier and is distributed on the fine sugar alcohol body, the bed temperature that the sweet spraying of control knob disperses is 35~50 ℃, and the sweet even spraying of knob 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 ℃, and the maltodextrin spray drying granulation is on the noncrystalline fluffy body of sugar alcohol; Obtain fluffy the shape product that even sugariness is modified.
Embodiment 1:
5 kilograms of maltodextrins and deionized water are dissolved in a stainless steel heating reaction pot for 20 kilograms, knob sweet 0.72 kilogram and deionized water are also dissolved in another stainless steel heating reaction pot for 20 kilograms, material is heated to 62 ℃ by chuck in the pot, start stirring, add 1 kilogram of active carbon respectively, be incubated 30 minutes, filter while hot, filtrate collects in the storage tank of chuck insulation stand-by respectively; With 64.28 kilograms of Dextrose Monohydrates, 25 kilograms of D-sorbites, 5 kilograms of oligoisomaltoses, pulverizing reaches 130 orders through pulverizer, be sent in the spray-fluidized bed apparatus, Dextrose Monohydrate, the mixed material of D-sorbite and oligoisomaltose enters the fluidized bed with spraying with malleation from the bottom of fluidized bed with spraying and quickens from bottom to top and flows, 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 sweet solution of the above-mentioned knob that refines continuously earlier and is distributed on the fine sugar alcohol body, control fluidized-bed layer temperature is 35~50 ℃, the multiple spot even spraying is disperseed, after operation is finished, improve bed temperature to 50~80 ℃ again, at Dextrose Monohydrate, D-sorbite, after the mixing of oligoisomaltose alcohol fluidisation loses surface crystallization water, pump into the above-mentioned maltodextrin solution that refines, continuously spray drying granulation, control air quantity and mist flow well, obtain the fluffy granular product that even sugariness is modified.
Embodiment 2:
6 kilograms of maltodextrins and deionized water are dissolved in a stainless steel heating reaction pot for 21 kilograms, knob sweet 1.45 kilograms and deionized water are also dissolved in another stainless steel reaction pot for 24 kilograms, material is heated to 52 ℃ by chuck in the pot, start stirring, add 2 kilograms of active carbons respectively, be incubated 30 minutes, filter while hot, filtrate collects in the storage tank of chuck insulation stand-by respectively; With 69 kilograms of Dextrose Monohydrates, 15 kilograms of D-sorbites, 8.55 kilograms of oligoisomaltoses, reach 150 orders through pulverizing, be sent to and carry out the fluidisation mixing in the spray-fluidized bed apparatus, Dextrose Monohydrate, the mixed material of D-sorbite and oligoisomaltose enters the fluidized bed with spraying with malleation from the bottom of fluidized bed with spraying and quickens from bottom to top and flows, 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 sweet solution of the above-mentioned knob 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 finished, improve bed temperature to 50~80 ℃ again, after making the mixing of above-mentioned various sugar alcohol alcohol 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 the fluffy granular product that even sugariness is modified.
Embodiment 3:
7 kilograms of maltodextrins and deionized water are dissolved in a stainless steel heating reaction pot for 22 kilograms, knob sweet 2.16 kilograms and deionized water are also dissolved in another stainless steel heating reaction pot for 25 kilograms, material is heated to 60 ℃ by chuck in the pot, start stirring, add 3.0 kilograms of active carbons respectively, be incubated 30 minutes, filter while hot, filtrate collects in the storage tank of chuck insulation stand-by respectively; With 63 kilograms of Dextrose Monohydrates, 20 kilograms of D-sorbites, 7.84 kilograms of oligoisomaltoses, pulverizing reaches 160 orders through pulverizer, be sent in the spray-fluidized bed apparatus, with Dextrose Monohydrate, the mixed material of D-sorbite and oligoisomaltose enters the fluidized bed with spraying with malleation from the bottom of fluidized bed with spraying and quickens from bottom to top and flows, 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 sweet solution of the above-mentioned knob 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 finished, improve bed temperature to 50~80 ℃ again, after the mixing of above-mentioned various sugar alcohol alcohol fluidisations loses surface crystallization water, pump into the above-mentioned maltodextrin solution that refines, continuously spray drying granulation, control air quantity and mist flow well, obtain the fluffy granular product that even sugariness is modified.
Embodiment 4:
4 kilograms of Dextrose Monohydrates and deionized water are dissolved in a stainless steel heating reaction pot for 20 kilograms, 25 kilograms also another dissolves in stainless steel heating reaction pot with knob sweet 2.88 kilograms and deionized water, material is heated to 80 ℃ by chuck in the pot, start stirring, add 3.0 kilograms of active carbons respectively, be incubated 35 minutes, filter while hot, filtrate collects in the storage tank of chuck insulation stand-by respectively; With 52 kilograms of Dextrose Monohydrates, 29 kilograms of D-sorbites, 12.12 kilograms of oligoisomaltoses, pulverizing reaches 180 orders through pulverizer, be sent to fluidisation in the spray-fluidized bed apparatus, the mixed material of above-mentioned various sugar alcohols entered the fluidized bed with spraying and quicken from bottom to top from the bottom of fluidized bed with spraying with malleation flow, 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 sweet solution of the above-mentioned knob 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 finished, improve bed temperature to 50~80 ℃ again, after above-mentioned various sugar alcohol alcohol fluidisations lose surface crystallization water, pumping into the above-mentioned maltodextrin solution that refines, the combination drying granulation of spraying continuously, control air quantity and mist flow well, obtain the fluffy granular product that even sugariness is adornd.
Embodiment 5:
8 kilograms of Dextrose Monohydrates and deionized water are dissolved in a stainless steel heating reaction pot for 25 kilograms, knob sweet 4.32 kilograms and deionized water are also dissolved in another stainless steel heating reaction pot for 29 kilograms, material is heated to 62 ℃ by chuck in the pot, start stirring, add 3 kilograms of active carbons respectively, be incubated 30 minutes, filter while hot, filtrate collects in the storage tank of chuck insulation stand-by respectively; With 50 kilograms of Dextrose Monohydrates, 25.68 kilograms of D-sorbites, 12 kilograms of oligoisomaltoses, pulverizing reaches 130 orders through pulverizer, be sent in the spray-fluidized bed apparatus, with Dextrose Monohydrate, the mixed material of D-sorbite and oligoisomaltose enters the fluidized bed with spraying with malleation from the bottom of fluidized bed with spraying and quickens from bottom to top and flows, 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 sweet solution of the above-mentioned knob that refines continuously earlier and is distributed on the fine sugar alcohol body, control fluidized-bed layer temperature is 35~50 ℃, the multiple spot even spraying is disperseed, after operation is finished, improve bed temperature to 50~80 ℃ again, at xylitol, D-sorbite, after the mixing of oligoisomaltose alcohol fluidisation loses surface crystallization water, pump into the above-mentioned maltodextrin solution that refines, continuously spray drying granulation, control air quantity and mist flow well, obtain the fluffy granular product that even sugariness is modified.
After testing, the fluffy granular composite low-sugar low-calorie sweetening agent that adopts technical solution of the present invention to obtain, its main performance index sees Table 1.
Table 1
Test item | Embodiment 1 | Embodiment 2 | Embodiment 3 | Embodiment 4 | Embodiment 5 |
Particle size | 30~60 orders | 30~60 orders | 30~60 orders | 30~60 orders | 30~60 orders |
Sugariness (sucrose contrast) | 50 times | 100 times | 150 times | 200 times | 300 times |
Outward appearance | White particle | White particle | White particle | White particle | White particle |
Bulk density (g/mm 3) | ??0.60 | ??0.62 | ??0.63 | ??0.65 | ??0.66 |
The stability test of 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 sweet taste material product of the embodiment of the invention was stored 3 years at normal temperatures, phenomenons such as rotten and sugariness reduction occur, and stability is very superior.
The sugariness degree of modification of fluffy granular composite low-sugar low-calorie sweetening agent of the present invention, according to the sweet adjustment in consumption of knob, in use unrestricted, usually select the common sucrose sugariness for use 50~300 times, the use needs that relatively are fit to food enterprise, form according to prescription, under same sugariness situation, people only are 1/50,1/300 of sucrose to the absorption of heat, low-sugar low-calorie sweetening agent is the sweet taste product of low-calorie, and this sweet taste material can not cause blood sugar to raise, satisfy three high crowds, the healthy people's of pursuit needs.
Show obviously that to sum up the present invention adopts scientific formula, uses advanced science and technology technology and method, products obtained therefrom does not have smell, do not have color, and is soluble in water, and it is very convenient that this fluffy granular low-sugar low-calorie sweetening agent is used.Granularity, molten speed, mouthfeel, sugariness all are much better than the prior art value, and the manufacturing process flow of science is simple and easy to do, are fit to very much large-scale production, are worth wide popularization and application in the field of business.
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 improvements and modifications, these improvements and modifications also should be considered as protection scope of the present invention.
Claims (5)
1. a composite sugar-free low-calorie sweetener is characterized in that comprising following composition (percentage by weight): Dextrose Monohydrate 50~69%, D-sorbite 15~30%, oligoisomaltose 5~13%, maltodextrin 4~8%, knob sweet 0.7~4.32%.
2. a kind of composite sugar-free low-calorie sweetener according to claim 1 is characterized in that its component has following percentage by weight: Dextrose Monohydrate 64.28%, D-sorbite 25%, oligoisomaltose 5%, maltodextrin 5%, knob sweet 0.72%.
3. the manufacture method of the described a kind of composite sugar-free low-calorie sweetener of claim 1 is characterized in that: comprise following processing step---
1. with maltodextrin, knob is sweet joins respectively in the heating container, add deionized water respectively and mix;
2. be warming up to 50~80 ℃ of dissolvings respectively, and stir;
3. add active carbon respectively in above-mentioned maltodextrin solution and the sweet solution of knob, be incubated 25~30 minutes, filter while hot, filtrate is pooled in the storage tank of heat tracing stand-by respectively;
4. with Dextrose Monohydrate, D-sorbite and oligoisomaltose are put in the spray-fluidized bed apparatus after pulverizing, Dextrose Monohydrate, the mixed material of D-sorbite and oligoisomaltose enters the fluidized bed with spraying with malleation from the bottom of fluidized bed with spraying and quickens from bottom to top and flows, 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 sweet solution of the above-mentioned knob 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 composite low-sugar low-calorie sweetening agent continuously.
4. the manufacture method of a kind of composite sugar-free low-calorie sweetener according to claim 3 is characterized in that: with maltodextrin, knob is sweet joins 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, filtrate is pooled to respectively in the storage tank that has heat tracing; With Dextrose Monohydrate, D-sorbite and oligoisomaltose reach 120~180 orders through pulverizing, be sent in the spray-fluidized bed apparatus, the mixed material of above-mentioned various sugar alcohols entered the fluidized bed with spraying and quicken from bottom to top from the bottom of fluidized bed with spraying with malleation flow, 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, control fluidized-bed layer temperature is at 35~80 ℃, the multiple spot spray gun of fluid bed sidepiece is sprayed the sweet solution of the above-mentioned knob that refines continuously earlier 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 composite low-sugar low-calorie sweetening agent continuously.
5. the manufacture method of a kind of composite low-sugar low-calorie sweetening agent according to claim 4, it is characterized in that: the bed temperature scope of described fluidized bed with spraying is 35~80 ℃, wherein the bed temperature of the sweet spraying dispersion of phase I knob is 35~50 ℃, and the bed temperature of second stage maltodextrin mist projection granulating is 50~80 ℃.
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Cited By (2)
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CN102424777A (en) * | 2011-12-20 | 2012-04-25 | 苏州工业园区尚融科技有限公司 | Production method for low-sugar grain alcohol fermentation beverage |
EP2568816A4 (en) * | 2010-05-12 | 2015-09-16 | Cargill Inc | Sweetener compositions with reduced bitter off taste and methods of preparing |
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US20050208190A1 (en) * | 2004-03-16 | 2005-09-22 | Kraft Foods Holdings, Inc. | Method for drying neotame with co-agents |
US20080069936A1 (en) * | 2006-09-18 | 2008-03-20 | ISON Renny | Cohesive non-free flowing sweeetener compositions containing a hygroscopic gluing agent and a desiccant |
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Cited By (2)
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EP2568816A4 (en) * | 2010-05-12 | 2015-09-16 | Cargill Inc | Sweetener compositions with reduced bitter off taste and methods of preparing |
CN102424777A (en) * | 2011-12-20 | 2012-04-25 | 苏州工业园区尚融科技有限公司 | Production method for low-sugar grain alcohol fermentation beverage |
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