CN101810313B - Dessert sweetener and production process - Google Patents
Dessert sweetener and production process Download PDFInfo
- Publication number
- CN101810313B CN101810313B CN2009102503907A CN200910250390A CN101810313B CN 101810313 B CN101810313 B CN 101810313B CN 2009102503907 A CN2009102503907 A CN 2009102503907A CN 200910250390 A CN200910250390 A CN 200910250390A CN 101810313 B CN101810313 B CN 101810313B
- Authority
- CN
- China
- Prior art keywords
- xylitol
- spraying
- fluidized bed
- sucralose
- bed
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Confectionery (AREA)
Abstract
The invention relates to a dessert sweetener and a production process. The dessert sweetener comprises the following components: 18-22 percent of xylitol, 0.037-0.045 percent of sucralose, 37-41.99 percent of sorbitol and 37-42 percent of erythritol. The process comprises the following steps of: respectively adding 5% xylitol and sucralose to a heating container, respectively adding deionized water and mixing, increasing the temperature to dissolve; respectively adding active carbon to the solution; filtering before cooling and respectively converging filtrate to a storage tank; enabling the crushed mixture of the xylitol, the sorbitol and the erythritol to enter the bed from the bottom of a spraying fluidized bed under positive pressure and flow at a high speed from bottom to top; applying negative pressure at the upper part of the spraying fluidized bed to vibrate from top to bottom so that materials are vertically boiled in the bed; continuously spraying and dispersing the refined sucralose solution to superfine sugar alcohol bodies by a multi-point spray gun at one side of the fluidized bed; and then; pumping the xylitol solution in, continuously spraying and drying to obtain a sugarless dessert sweetening agent. The preparation flows are simple and easy to operate, and the sweetness of the product is 0.70-0.74 times that of common sugar.
Description
Technical field
The present invention relates to a kind of edible dining table sweetener, relate in particular to a kind of fluffy granular composite sugar-free dessert sweetener and production technology thereof.
Background technology
The increase of Along with people's because of too much bringing disease with sugar, people's demand safety, healthy Sugarless type dining table sweetener; 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 under the prerequisite that satisfies sugariness height, empty calory, and occupation modeization, with cane-sugar taste safety and Health Sugarless type dessert sweetener roughly the same.
Summary of the invention
The objective of the invention is to overcome the deficiency that prior art exists, a kind of fluffy granular composite sugar-free dessert sweetener and production technology thereof are 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:
Dessert sweetener, characteristics are to comprise following composition (percentage by weight): xylitol 18～22%, Sucralose 0.037～0.045%, D-sorbite 37～41.99%, antierythrite 37～42%.
Further, above-mentioned dessert sweetener, wherein, xylitol 18%, Sucralose 0.0374%, D-sorbite 41.9626%, antierythrite 40%.
The production technology of dessert sweetener of the present invention comprises following processing step:
1. with 5% xylitol, Sucralose joins respectively in the heating container, adds deionized water respectively and mixes;
2. be warming up to 52～80 ℃ of dissolvings respectively, and stir;
3. add active carbon respectively in above-mentioned xylitol 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. put in the spray-fluidized bed apparatus after xylitol, antierythrite and D-sorbite being pulverized; The mixed material of above-mentioned various sugar alcohols 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 xylitol solution that refines again, spray-drying obtains the fluffy granular composite sugar-free dessert sweetener continuously.
Again further, the production technology of above-mentioned dessert sweetener, the xylitol with 5%, Sucralose join respectively in the heating 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; Xylitol, antierythrite and D-sorbite reach 120～180 orders through pulverizing; Be sent in the spray-fluidized bed apparatus; The mixed material of above-mentioned various sugar alcohols 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 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 xylitol solution that refines again, spray drying granulation obtains the fluffy granular composite sugar-free dessert sweetener continuously.
Again further; The production technology of above-mentioned dessert sweetener; The bed temperature scope of said fluidized bed with spraying is 35～80 ℃, and wherein the bed temperature of phase I Sucralose spraying dispersion is 35～50 ℃, and the bed temperature of second stage xylitol mist projection granulating is 50～80 ℃.
Again further, the production technology of above-mentioned dessert sweetener, 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 xylitol 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 xylitol, D-sorbite, antierythrite is primary raw material; Modify uniformly and coat through preparation method to sugariness, make product sweetness reach 0.70～0.74 times of common sucrose, products obtained therefrom does not have smell, does not have color; Soluble in water; This fluffy granular composite sugar-free dessert sweetener is easy to use, and 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
Dessert sweetener, its composition is: xylitol 18～22%, Sucralose 0.037～0.045%, D-sorbite 37～41.99%, antierythrite 37～42%.Ideal formulations is: xylitol 18%, Sucralose 0.0374%, D-sorbite 41.9626%, antierythrite 40%.
As shown in Figure 1, the preparation technology of dessert sweetener: at first, the xylitol with 5%, Sucralose join 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 xylitol 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; Put into after xylitol, antierythrite and D-sorbite pulverized 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 xylitol, antierythrite and D-sorbite 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; After fluidisation loses surface crystallization water, pump into the above-mentioned xylitol solution that refines at mixing sugar alcohol again, continuously spray drying granulation; The bed temperature of xylitol mist projection granulating controlled well is 50～80 ℃, and the xylitol spray drying granulation is on the noncrystalline fluffy body of sugar alcohol; Obtain even sugariness and modify fluffy good shape product.
Embodiment 1:
6 kilograms of xylitols and deionized water are dissolved in a stainless steel reacting by heating pot for 21 kilograms; 0.0374 kilogram of Sucralose and deionized water are also dissolved in another stainless steel reacting by heating pot for 22 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; 18 kilograms of xylitols, 40 kilograms of antierythrites, 41.9626 kilograms of D-sorbites; Pulverize through pulverizer and to reach 130 orders, be sent in the spray-fluidized bed apparatus, the mixed material of above-mentioned various sugar alcohols is got into the fluidized bed with spraying and quickens from bottom to top from the bottom of fluidized bed with spraying with malleation flow; 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 earlier will the above-mentioned sucralose solution that refines continuously spraying be distributed on the fine sugar alcohol body, controlling the fluidized-bed layer temperature is 35～50 ℃; The multiple spot even spraying is disperseed; After operation is accomplished, improve bed temperature to 50～80 ℃ again, above-mentioned various sugar alcohols alcohol fluidisations mix lose surface crystallization water after; Pump into the above-mentioned xylitol solution that refines; Continuous spray drying granulation is controlled air quantity and mist flow well, obtains even sugariness and modifies good fluffy granular product.
Embodiment 2:
6 kilograms of xylitols and deionized water are dissolved in a stainless steel reacting by heating pot for 25 kilograms; 0.0391 kilogram of Sucralose and deionized water are also dissolved in another stainless steel reaction pot for 20 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; 19 kilograms of xylitols, 41.9609 kilograms of antierythrites, 40 kilograms of D-sorbites; Reach 150 orders through pulverizing, to be sent to and to carry out fluidisation in the spray-fluidized bed apparatus and mix, the mixed material of above-mentioned various sugar alcohols to be got into the fluidized bed with spraying and quickens from bottom to top from the bottom of fluidized bed with spraying with malleation flow; 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 earlier will the above-mentioned sucralose solution that refines continuously spraying be distributed on the fine sugar alcohol body, control 35～40 ℃ of fluidized-bed layer temperature; Even spraying is disperseed; After operation is accomplished, improve bed temperature to 50～80 ℃ again, after above-mentioned various sugar alcohol alcohol fluidisation being mixed lose surface crystallization water; Pumping into the above-mentioned xylitol solution that refines; Continuous spray granulating and drying is controlled air quantity and mist flow well, obtains even sugariness and modifies good fluffy granular product.
Embodiment 3:
6 kilograms of xylitols and deionized water are dissolved in a stainless steel reacting by heating pot for 26 kilograms; 0.0408 kilogram of Sucralose and deionized water are also dissolved in another stainless steel reacting by heating pot for 20 kilograms, and material is heated to 60 ℃ by chuck in the pot, starts stirring; Add 3.0 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; 20 kilograms of xylitols, 42 kilograms of antierythrites, 37.9592 kilograms of D-sorbites; Pulverize through pulverizer and to reach 160 orders, be sent in the spray-fluidized bed apparatus, the mixed material of above-mentioned various sugar alcohols is got into the fluidized bed with spraying and quickens from bottom to top from the bottom of fluidized bed with spraying with malleation flow; 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 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, controls 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, above-mentioned various sugar alcohols alcohol fluidisations mix lose surface crystallization water after; Pump into the above-mentioned xylitol solution that refines; Continuous spray drying granulation is controlled air quantity and mist flow well, obtains even sugariness and modifies good fluffy granular product.
Embodiment 4:
6 kilograms of xylitols and deionized water are dissolved in a stainless steel reacting by heating pot for 25 kilograms; 20 kilograms also another dissolves in stainless steel reacting by heating pot with deionized water with 0.0425 kilogram of Sucralose, 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; 21 kilograms of xylitols, 39.95975 kilograms of antierythrites, 40 kilograms of D-sorbites; Pulverize through pulverizer and to reach 180 orders, be sent to fluidisation in the spray-fluidized bed apparatus, the mixed material of above-mentioned various sugar alcohols is got into the fluidized bed with spraying and quickens from bottom to top from the bottom of fluidized bed with spraying with malleation flow; 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 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, controls 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 above-mentioned various sugar alcohols alcohol fluidisations lose surface crystallization water; Pumping into the above-mentioned xylitol solution that refines; Continuous Spray Mixing drying-granulating is controlled air quantity and mist flow well, obtains the good fluffy granular product of even sugariness decorations.
Embodiment 5:
6 kilograms of xylitols and deionized water are dissolved in a stainless steel reacting by heating pot for 24 kilograms; 20 kilograms also another dissolves in stainless steel reacting by heating pot with deionized water with 0.0442 kilogram of Sucralose, 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; 22 kilograms of xylitols, 38 kilograms of antierythrites, 39.9558 kilograms of D-sorbites; Pulverize through pulverizer and to reach 180 orders, be sent to fluidisation in the spray-fluidized bed apparatus, the mixed material of above-mentioned various sugar alcohols is got into the fluidized bed with spraying and quickens from bottom to top from the bottom of fluidized bed with spraying with malleation flow; 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 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, controls 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 above-mentioned various sugar alcohols alcohol fluidisations lose surface crystallization water; Pumping into the above-mentioned xylitol solution that refines; Continuous Spray Mixing drying-granulating is controlled air quantity and mist flow well, obtains the good fluffy granular product of even sugariness decorations.
Through detecting, adopt the fluffy granular composite sugar-free dessert sweetener of technical scheme acquisition of the present invention, its main performance index is seen 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) | 0.70 doubly | 0.71 doubly | 0.72 doubly | 0.73 doubly | 0.74 doubly |
| Outward appearance | White particle | White particle | White particle | White particle | White particle |
| Bulk density (g/mm 3) | 0.60 | 0.62 | 0.63 | 0.66 | 0.66 |
The stability test of sweetener is to check sweetener to guarantee the ability that undergoes no deterioration within a certain period of time, and the dessert sweetener 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.
The sugariness degree of modification of fluffy granular composite sugar-free dessert sweetener of the present invention will be according to the adjustment of Sucralose in consumption, select the common sucrose sugariness usually for use 0.70～0.74 times; Relatively be fit to the use needs of food enterprise dessert, form, under same sugariness situation according to prescription; People are almost nil to the absorption of heat, and this composite sugar-free dessert sweetener can not cause blood sugar to raise, not carious tooth; Be fit to the diabetes patient, satisfy three high crowds, pursue healthy needs of people.
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 granule-shaped sugar-free dessert sweetener is used.Granularity, molten speed, mouthfeel, sugariness all are much better than the prior art value, and the scientific preparation process simple flow is prone to row, 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 improvement and retouching, these improvement and retouching also should be regarded as protection scope of the present invention.
Claims (4)
1. dessert sweetener is characterized in that comprising following percentage by weight composition: xylitol 18～22%, Sucralose 0.037～0.045%, D-sorbite 37～41.99%, antierythrite 37～42%; Its preparation method comprises following processing step:
1. with 6% xylitol, Sucralose joins respectively in the heating container, adds deionized water respectively and mixes;
2. be warming up to 52～80 ℃ of dissolvings respectively, and stir;
3. add active carbon respectively in above-mentioned xylitol 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. put in the spray-fluidized bed apparatus after xylitol, antierythrite and D-sorbite being pulverized; The mixed material of xylitol, antierythrite and D-sorbite 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 bed temperature scope of fluidized bed with spraying is 35～80 ℃; Wherein the bed temperature of phase I Sucralose spraying dispersion is 35～50 ℃; The bed temperature of second stage xylitol mist projection granulating is 50～80 ℃, and 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 mixed material of fine xylitol, antierythrite and D-sorbite, pumps into the above-mentioned xylitol solution that refines again; Spray-drying obtains the fluffy granular composite sugar-free dessert sweetener continuously.
2. dessert sweetener according to claim 1 is characterized in that its composition has following percentage by weight: xylitol 18%, Sucralose 0.0374%, D-sorbite 41.9626%, antierythrite 40%.
3. the production technology of the described dessert sweetener of claim 1 is characterized in that: comprise following processing step---
1. with 6% xylitol, Sucralose joins respectively in the heating container, adds deionized water respectively and mixes;
2. be warming up to 52～80 ℃ of dissolvings respectively, and stir;
3. add active carbon respectively in above-mentioned xylitol 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. put in the spray-fluidized bed apparatus after xylitol, antierythrite and D-sorbite being pulverized; The mixed material of xylitol, antierythrite and D-sorbite 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 bed temperature scope of fluidized bed with spraying is 35～80 ℃; Wherein the bed temperature of phase I Sucralose spraying dispersion is 35～50 ℃; The bed temperature of second stage xylitol mist projection granulating is 50～80 ℃, and 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 mixed material of fine xylitol, antierythrite and D-sorbite, pumps into the above-mentioned xylitol solution that refines again; Spray-drying obtains the fluffy granular composite sugar-free dessert sweetener continuously.
4. the production technology of dessert sweetener according to claim 3, it is characterized in that: the xylitol with 6%, Sucralose join 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; Xylitol, antierythrite and D-sorbite reach 120～180 orders through pulverizing; Be sent in the spray-fluidized bed apparatus; The mixed material of above-mentioned various sugar alcohols 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 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 mixed material of fine xylitol, antierythrite and D-sorbite; After the goods fluid mixing loses surperficial moisture content; Pump into the above-mentioned xylitol solution that refines again, spray drying granulation obtains the fluffy granular composite sugar-free dessert sweetener continuously.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009102503907A CN101810313B (en) | 2009-12-07 | 2009-12-07 | Dessert sweetener and production process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009102503907A CN101810313B (en) | 2009-12-07 | 2009-12-07 | Dessert sweetener and production process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101810313A CN101810313A (en) | 2010-08-25 |
| CN101810313B true CN101810313B (en) | 2012-12-12 |
Family
ID=42617804
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009102503907A Expired - Fee Related CN101810313B (en) | 2009-12-07 | 2009-12-07 | Dessert sweetener and production process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101810313B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102960823A (en) * | 2012-11-30 | 2013-03-13 | 苏州工业园区尚融科技有限公司 | Compound sweetener suitable for sour drinks and preparation method of sweetener |
| CN102960824A (en) * | 2012-11-30 | 2013-03-13 | 苏州工业园区尚融科技有限公司 | Compound sweetener applied sour beverages and preparation method of sweetener |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1254522A (en) * | 1999-12-09 | 2000-05-31 | 北京恒毅利科贸有限责任公司 | Method for preparing granular flavouring enriched food and its product |
| CN101181050A (en) * | 2007-12-19 | 2008-05-21 | 苏州苏克瑞甜品科技有限公司 | Sucrose succedaneum and preparation method thereof |
| CN101253968A (en) * | 2008-04-15 | 2008-09-03 | 苏州苏克瑞甜品科技有限公司 | Granular sugar-free sweetening agent and method of preparing the same |
-
2009
- 2009-12-07 CN CN2009102503907A patent/CN101810313B/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1254522A (en) * | 1999-12-09 | 2000-05-31 | 北京恒毅利科贸有限责任公司 | Method for preparing granular flavouring enriched food and its product |
| CN101181050A (en) * | 2007-12-19 | 2008-05-21 | 苏州苏克瑞甜品科技有限公司 | Sucrose succedaneum and preparation method thereof |
| CN101253968A (en) * | 2008-04-15 | 2008-09-03 | 苏州苏克瑞甜品科技有限公司 | Granular sugar-free sweetening agent and method of preparing the same |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101810313A (en) | 2010-08-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101897424B (en) | Fluffy granular compound sugarless dining table sweetener and preparation method thereof | |
| CN101874599B (en) | Composite low-sugar low-calorie dining-table sweetener and preparation method thereof | |
| CN101715941B (en) | Dinning-table sweetener and production process thereof | |
| CN101897426A (en) | Granular composite sugar-free sweetener and preparation method thereof | |
| CN101897422A (en) | Fluffy granular compound low-sugar low-calorie sweetening agent and preparation method thereof | |
| CN101874606B (en) | Fluffy granular composite sugar-free sweetener at dining table and preparation method thereof | |
| CN101874591A (en) | Fluffy granular composite low-sugar and low-calorie sweetener and preparation method thereof | |
| CN101874596B (en) | Composite sugar-free sweetener and preparation method thereof | |
| CN101874607B (en) | Granular composite low-sugar low-calorie sweetener and preparation method thereof | |
| CN101874594B (en) | Fluffy granular composite sugar-free sweetener and preparation method thereof | |
| CN101720911A (en) | Low-calorie dining table sweetener and production method thereof | |
| CN101874600B (en) | Granular composite low-sugar low-calorie dining table sweetener and preparation method thereof | |
| CN101874604B (en) | Fluffy granular composite low-sugar and low-calorie sweetener and preparation method thereof | |
| CN101874593A (en) | Fluffy granular composite sugar-free table sweetener and preparation method thereof | |
| CN101810302B (en) | Novel fluffy granular composite low-sugar low-calorie sweetening agent and preparing method thereof | |
| CN101874595B (en) | Composite sugar-free sweetener and preparation method thereof | |
| CN101874602B (en) | Fluffy granular composite low-sugar and low-calorie table sweetener and preparation method thereof | |
| CN101810313B (en) | Dessert sweetener and production process | |
| CN101874597B (en) | Fluffy granular composite sugar-free sweetener and preparation method thereof | |
| CN101810299B (en) | Composite sugar-free low-calorie sweetener and manufacturing method thereof | |
| CN101810305B (en) | Novel composite sugar-free table sweetener and production method thereof | |
| CN101810312B (en) | Moon cake sweetener and preparation method thereof | |
| CN101897421A (en) | Granular composite sugar-free sweetener and preparation method thereof | |
| CN101810309B (en) | Novel composite low-sugar low-calorie sweetener for dining table and manufacturing process thereof | |
| CN101810300B (en) | Composite low-sugar-content and low-calorie sweetening agent and manufacture method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121212 Termination date: 20211207 |