CN103098968A - Method for producing nutrition sugar by sugar producing material - Google Patents
Method for producing nutrition sugar by sugar producing material Download PDFInfo
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- CN103098968A CN103098968A CN2013100486138A CN201310048613A CN103098968A CN 103098968 A CN103098968 A CN 103098968A CN 2013100486138 A CN2013100486138 A CN 2013100486138A CN 201310048613 A CN201310048613 A CN 201310048613A CN 103098968 A CN103098968 A CN 103098968A
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Abstract
The invention discloses a method for producing nutrition sugar by a sugar producing material, and relates to the sugar production manufacture technical field. The method comprises the steps of juicing the raw materials, clarifying the cane juice, evaporating, boiling the sugar, crystallizing, purging and drying, the honey obtained by crystallizing and purging of the boiled sugar material is subjected to cleaning treatment, the honey is raw honey and machine syrup or molasses, the treated clean syrup is taken as the raw material for boiling the sugar paste; a sugar seed is placed in a crystallization tank, then the clean syrup is placed in the tank for boiling the sugar paste, the volume ratio of the sugar seed to the boiled sugar paste product is 1:2-3, when the concentration of the material in the tank is 104 Bx-106 Bx, the boiling is completed, the sugar paste is taken out, and the sugar paste is subjected to vacuum drying to obtain the product. The produced nutrition sugar contains the nutrition component of the sugarcane, the resource is fully utilized, the sugarcane sugar producing organic matter refuse discharge capacity is reduced, and the product has special fragrant smell of the sugarcane.
Description
Technical field
The present invention relates to Sugar Production manufacturing technology field, especially a kind of manufacture method of brown sugar sugar products.
Background technology
Existing Sugar Production manufacturing material goes the deimpurity while through boiling, crystallization in motion, purging mode, and the nutritional labeling that the human bodies such as part sucrose, all reduced sugars, xylo-oligosaccharide, low araban, galactooligosaccharide, beta glucan, phospholipoprotein, polyphenol chromocor class, amino acid, vitamin, organic acid need and human body Auto-regulator are in company with being removed.Brown sugar claims again brown granulated sugar, and brown granulated sugar is a kind of byproduct that obtains after raw massecuite crystallization in motion, purging in the sugaring manufacturing process, and main component is sucrose, a small amount of reduced sugar, honey, and nutritional labeling is low than brown sugar, and purity is high than brown sugar.Tradition brown sugar is manufactured and is rich in all nutritional labelings of sugarcane owing to not removing the impurity product, but the impurity content in product is high, is difficult to reach the QB/T2343.2 standard; Can remove the calcium ion in material with sodium carbonate, Sodium Polyacrylate method, but can increase sodium ion newly again, and the impurity such as sulfate radical, silicate, magnesium ion can't be removed, material can not effectively be utilized, residual a large amount of sulfate radicals in material when regulating PH to 2～3 isoelectric point sedimentation corrosivity Datong District with the concentrated sulfuric acid, electrode ionization adsorption and sedimentation method cost is high, efficient is low etc., and reason is difficult to use aborning.
Summary of the invention
The purpose of this invention is to provide a kind of harmful inorganic ash content that can either remove in the sugaring material, the sugaring material that can keep again nutritional labeling useful in material is made the method for nutrient sugar.
In order to reach the problems referred to above, the technical solution used in the present invention is: this sugaring material is made the method for nutrient sugar, comprise raw material extraction of the juice, sugarcane juice clarification, evaporate, boil sugar, crystallization in motion, purging and drying process, boil the honey that sugared back segment material sieves out through crystallization in motion, purging and carry out clarify process described, described honey is that second green molasses, second are washed honey or molasses, and the clear syrup that processing obtains is as the raw material of boiling massecuite; Put into sugar and plant in crystallizing tank, then put into described clear syrup boiling massecuite, described sugar is planted and the volume ratio of boiling massecuite finished product is 1:2 ~ 3; When material concentration in tank when being 104Bx ~ 106Bx boiling complete, emit massecuite, massecuite namely gets required product through vacuum drying;
The step of described clarify process is as follows:
A, dilution: honey is diluted to 60 Bx ~ 70Bx;
B, heating: the honey after dilution is heated to 70 ℃ ~ 80 ℃;
C, floating: the heating honey that compressed air the is passed into step B floating of getting blisters in floating device clears out the foam of floating;
D, sedimentation: form calcium monohydrogen phosphate-calcium phosphate network sedimentation in the honey of having removed foam with calcium hydroxide and the step C of phosphoric acid and 1.0 ~ 1.2 phosphoric acid equivalents, add again the suspended particulate impurity sedimentation in the auxiliary absorption of flocculant honey, obtain clearly syrup as the raw material of boiling massecuite.
In the technical scheme of the method for above-mentioned sugaring material manufacturing nutrient sugar, technical scheme can also be more specifically: the precipitum that produces in clarify process step D is carried out centrifugation, and the clear syrup that obtains is as the raw material that boils sugar.
Further, described phosphoric acid consumption is 800 ppm ~ 2400ppm, and described flocculant consumption is 2.5 ppm ~ 10ppm.
Further, the foam that clears out by floating in clarify process is formed powder through vacuum drying, described powder is added in massecuite.
Further, come the boiling massecuite by the triose cooking technology, brew temperatures is 68 ℃ ~ 73 ℃, pressure is-and 0.095Mpa ~-0.105Mpa.
Further, the purity that described sugar is planted is 65Ap ~ 85Ap, and the hammer degree is for being 80 Bx ~ 83Bx.
Owing to having adopted technique scheme, the present invention compared with prior art has following beneficial effect:
1, the boiling material improves approximately 8 Ap ~ 13Ap through purity after clarify process, and reduced viscosity is conducive to boiling and sucrose molecule crystallization;
2, boiling material inorganic impurity content is lower than national standard, and the boiling massecuite can keep non crystallized nutritional labeling in material without purging, and resource is fully utilized;
3, the boiling massecuite does not produce molasses by vacuum drying, and contamination-free produces;
4, the powder that foam-drying is formed adds in massecuite, can further increase the surface-active organic substance in commerieal sugar.
The specific embodiment
Embodiment 1
The common sulfurous method sugar refining technology of the present embodiment take the employing sugarcane as raw material comprises raw material extracting sugarcane juice, clarification, evaporates, boils sugar, crystallization in motion, purging and drying process as the basis.To the clarify process method of boiling sugared material be: the purity that intermediate massecuite is sieved out through purging is that the second of 46.5Ap is washed sweet stream and added 40m
3Interlayer Steam Heating thinning tank in, be diluted to 63.0Bx with 65 ℃ of sugar refining technology water, then with steam, the honey of dilution be heated to 78 ~ 80 ℃ and flow into floating devices, pass into the floating of getting blisters in the honey of heating with compressed air, clear out the foam of floating; The honey of having removed foam is added in accelerated clarifier, add accelerated clarifier to form calcium monohydrogen phosphate-calcium phosphate network sedimentation with 1200ppm phosphoric acid and 1300ppm calcium hydroxide, simultaneously stream adds the auxiliary absorption of 3.5ppm flocculant suspended particulate impurity sedimentation in the accelerated clarifier, and the purity that obtains after sedimentation is the clear syrup of 58.3Ap; The precipitum that accelerated clarifier is discharged carries out centrifugation with tripod pendulum type batch centrifugal, and obtaining purity is the clear syrup of 58.5Ap.The purity that intermediate massecuite is sieved out through purging is that the second green molasses stream of 43.5Ap adds 40 m
3Interlayer Steam Heating thinning tank in, be diluted to 60.0Bx with 65 ℃ of sugar refining technology water, then with steam, dilution close be heated to 76 ~ 78 ℃ and flow into floating devices, pass into the floating of getting blisters in the honey of heating with compressed air, clear out the foam of floating; The honey of having removed foam is added in accelerated clarifier, add accelerated clarifier to form calcium monohydrogen phosphate-calcium phosphate network sedimentation with 1600ppm phosphoric acid and 1800ppm calcium hydroxide, simultaneously stream adds the auxiliary absorption of 5ppm flocculant suspended particulate impurity sedimentation in the accelerated clarifier, and the purity that obtains after sedimentation is the clear syrup of 56.1Ap; The precipitum that accelerated clarifier is discharged carries out centrifugation with tripod pendulum type batch centrifugal, and obtaining purity is the clear syrup of 56.4Ap.Press triose cooking technology boiling 30 m
3Massecuite, first suction purity is that 65Ap, hammer degree are 10 m of 80Bx in the crystallizing tank
3Sugar is planted (sugar is planted and also claimed sucrose nucleus bed material), then add that purity is the clear syrup boiling of 58.3Ap and 58.7Ap after clarify process in the tank, add again that purity is the clear syrup boiling of 56.3Ap and 56.8Ap after clarify process, brew temperatures is controlled to be 68 ℃ ~ 70 ℃, pressure is controlled at-0.095Mpa ~-the 0.105Mpa scope in, boiling 7 hours, adding the clear syrup cumulative volume in tank in boiling is 35 m
3, the moisture that in this process, in tank, material contains is evaporated, and material reaches 30 m in tank
3And emit massecuite when material concentration is 106Bx, massecuite namely obtains nutrient sugar after vacuum drying is cooling.
Embodiment 2
The common sulfurous method sugar refining technology of the present embodiment take the employing sugarcane as raw material comprises raw material extracting sugarcane juice, clarification, evaporates, boils sugar, crystallization in motion, purging and drying process as the basis.To the clarify process method of boiling sugared material be: the purity that intermediate massecuite is sieved out through purging is that the second of 46.0Ap is washed sweet stream and added 40 m
3Interlayer Steam Heating thinning tank in, be diluted to 62.5Bx with 65 ℃ of sugar refining technology water, then with steam, the honey of dilution be heated to 70 ~ 72 ℃ and flow into floating devices, pass into the floating of getting blisters in the honey of heating with compressed air, clear out the foam of floating; The honey of having removed foam is added in accelerated clarifier, flow into accelerated clarifier with 1000ppm phosphoric acid and 1200ppm calcium hydroxide and form calcium monohydrogen phosphate-calcium phosphate network sedimentation, simultaneously stream adds the auxiliary absorption of 2.5ppm flocculant suspended particulate impurity sedimentation in the accelerated clarifier, and the purity that obtains after sedimentation is the clear syrup of 57.8Ap; The precipitum that accelerated clarifier is discharged carries out centrifugation with tripod pendulum type batch centrifugal, and obtaining purity is the clear syrup of 58.0Ap.The purity that intermediate massecuite is sieved out through purging is that the second green molasses stream of 42.0Ap adds 40 m
3Interlayer Steam Heating thinning tank in, be diluted to 63.0Bx with 65 ℃ of sugar refining technology water, then with steam, the honey of dilution be heated to 76 ~ 78 ℃ and flow into floating devices, pass into the floating of getting blisters in the honey of heating with compressed air, clear out the foam of floating; The honey of having removed foam is added in accelerated clarifier, flow into accelerated clarifier with 1800ppm phosphoric acid and 2000ppm calcium hydroxide and form calcium monohydrogen phosphate-calcium phosphate network sedimentation, simultaneously stream adds the auxiliary absorption of 8ppm flocculant suspended particulate impurity sedimentation in the accelerated clarifier, and the purity that obtains after sedimentation is the clear syrup of 54.3Ap; The precipitum that accelerated clarifier is discharged carries out centrifugation with tripod pendulum type batch centrifugal, and obtaining purity is the clear syrup of 54.5Ap.Press triose cooking technology boiling 30 m
3Massecuite, first suction purity is that 70Ap, hammer degree are 12 m of 80.5Bx in the crystallizing tank
3Sugar is planted, then add that purity is the clear syrup boiling of 57.8Ap and 58.0Ap after clarify process in the tank, add again that purity is the clear syrup boiling of 54.3Ap and 54.5Ap after clarify process, brew temperatures is controlled to be 70 ℃ ~ 72 ℃, pressure is controlled at-0.095Mpa ~-the 0.105Mpa scope in, boiling 7 hours, adding the clear syrup cumulative volume in tank in boiling is 32m
3, the moisture that in this process, in tank, material contains is evaporated, and material reaches 30 m in tank
3And emit massecuite when material concentration is 105.5Bx, massecuite namely obtains nutrient sugar after vacuum drying is cooling.
Embodiment 3
The present embodiment to be to adopt sugarcane as the common sulfurous method sugar refining technology of raw material is the basis, and comprising raw material extracting sugarcane juice, clarification, evaporation, three is to boil sugar, crystallization in motion, purging and drying process.To the clarify process method of boiling sugared material be: the purity that intermediate massecuite is sieved out through purging is that the second of 50.3Ap is washed sweet stream and added 40 m
3Interlayer Steam Heating thinning tank in, be diluted to 70.0Bx with 65 ℃ of sugar refining technology water, then with steam, the honey of dilution be heated to 78 ~ 80 ℃ and flow into floating devices, pass into the floating of getting blisters in the syrup of heating with compressed air, clear out the foam of floating; The honey of having removed foam is added in accelerated clarifier, flow into accelerated clarifier with 800ppm phosphoric acid and 900ppm calcium hydroxide and form calcium monohydrogen phosphate-calcium phosphate network sedimentation, simultaneously stream adds the auxiliary absorption of 4.5ppm flocculant suspended particulate impurity sedimentation in the accelerated clarifier, and the purity that obtains after sedimentation is the clear syrup of 62.3Ap; The precipitum that accelerated clarifier is discharged carries out centrifugation with tripod pendulum type batch centrifugal, and obtaining purity is the clear syrup of 62.5Ap.The purity that intermediate massecuite is sieved out through purging is that the second green molasses stream of 45.2Ap adds 40 m
3Interlayer Steam Heating thinning tank in, be diluted to 64.0Bx with 65 ℃ of sugar refining technology water, then with steam, the honey of dilution be heated to 76 ~ 78 ℃ and flow into floating devices, pass into the floating of getting blisters in the honey of heating with compressed air, clear out the foam of floating; The honey of having removed foam is added in accelerated clarifier, flow into accelerated clarifier with 1200ppm phosphoric acid and 1350ppm calcium hydroxide and form calcium monohydrogen phosphate-calcium phosphate network sedimentation, simultaneously stream adds the auxiliary absorption of 5.5ppm flocculant suspended particulate impurity sedimentation in the accelerated clarifier, the purity that obtains after sedimentation is the clear syrup of 58.0Ap, the precipitum that accelerated clarifier is discharged carries out centrifugation with tripod pendulum type batch centrifugal, and obtaining purity is the clear syrup of 58.3AP.Press triose cooking technology boiling 30 m
3Massecuite, first suction purity is that 75Ap, hammer degree are 13 m of 81Bx in the crystallizing tank
3Sugar is planted, then add that purity is the clear syrup boiling of 62.3Ap and 62.5Ap after clarify process in the tank, add again that purity is the clear syrup boiling of 58.0Ap and 58.3Ap after clarify process, brew temperatures is controlled to be 71 ℃ ~ 73 ℃, pressure is controlled at-0.095Mpa ~-the 0.105Mpa scope in, boiling 7 hours, adding the clear syrup cumulative volume in tank in boiling is 28m
3, the moisture that in this process, in tank, material contains is evaporated, and material reaches 30m in tank
3And emit massecuite when material concentration is 104.0Bx, the foam that floating in clarify process is cleared out forms powder through vacuum drying, this powder is added in massecuite mix, and massecuite namely obtains nutrient sugar after vacuum drying is cooling.
Embodiment 4
The common sulfurous method sugar refining technology of the present embodiment take the employing sugarcane as raw material comprises raw material extracting sugarcane juice, clarification, evaporates, boils sugar, crystallization in motion, purging and drying process as the basis.To the clarify process method of boiling sugared material be: the purity that raw massecuite is sieved out through purging is that the molasses stream of 35.2Ap adds 40 m
3Interlayer Steam Heating thinning tank in, be diluted to 60.0Bx with 65 ℃ of sugar refining technology water, then with steam, dilution close be heated to 78 ~ 80 ℃ and flow into floating devices, pass into the floating of getting blisters in the honey of heating with compressed air, clear out the foam of floating; The honey of having removed foam is added in accelerated clarifier, flow into accelerated clarifier with 2000ppm phosphoric acid and 2200ppm calcium hydroxide and form calcium monohydrogen phosphate-calcium phosphate network sedimentation, simultaneously stream adds the auxiliary absorption of 7ppm flocculant suspended particulate impurity sedimentation in the accelerated clarifier, and the purity that obtains after sedimentation is the clear syrup of 47.5Ap.Press triose cooking technology boiling 30 m
3Massecuite, first suction purity is that 80Ap, hammer degree are 14 m of 82Bx in the crystallizing tank
3Sugar is planted, and adds then that purity is the clear syrup boiling of 47.5AP after clarify process in the tank, and brew temperatures is controlled to be 71 ℃ ~ 73 ℃, pressure is controlled at-0.095Mpa ~-the 0.105Mpa scope in, boiling 7 hours, adding the clear syrup cumulative volume in tank in boiling is 31m
3, the moisture that in this process, in tank, material contains is evaporated, and material reaches 30 m in tank
3And emit massecuite when material concentration is 105.5Bx, massecuite namely obtains nutrient sugar after vacuum drying is cooling.
Embodiment 5
The common sulfurous method sugar refining technology of the present embodiment take the employing sugarcane as raw material comprises raw material extracting sugarcane juice, clarification, evaporates, boils sugar, crystallization in motion, purging and drying process as the basis.To the clarify process method of boiling sugared material be: the purity that raw massecuite is sieved out through purging is that the molasses stream of 32.8Ap adds 40 m
3Interlayer Steam Heating thinning tank in, be diluted to 62.0Bx with 65 ℃ of sugar refining technology water, then with steam, the honey of dilution be heated to 76 ~ 78 ℃ and flow into floating devices, pass into the floating of getting blisters in the honey of heating with compressed air, clear out the foam of floating, it is standby that foam forms powder through vacuum drying; The honey of having removed foam is added in accelerated clarifier, flow into accelerated clarifier with 2400ppm phosphoric acid and 2500ppm calcium hydroxide and form calcium monohydrogen phosphate-calcium phosphate network sedimentation, simultaneously stream adds the auxiliary absorption of 10ppm flocculant suspended particulate impurity sedimentation in the accelerated clarifier, and the purity that obtains after sedimentation is the clear syrup of 45.2Ap.Press triose cooking technology boiling 30 m
3Massecuite, first suction purity is that 75Ap, hammer degree are 15 m of 83Bx in the crystallizing tank
3Sugar is planted, and adds then that purity is the clear syrup boiling of 45.2Ap after clarify process in the tank, and brew temperatures is controlled to be 68 ℃ ~ 70 ℃, pressure is controlled at-0.095Mpa ~-the 0.105Mpa scope in, boiling 7 hours, adding the clear syrup cumulative volume in tank in boiling is 28m
3, the moisture that in this process, in tank, material contains is evaporated, and material reaches 30 m in tank
3And emit massecuite when material concentration is 105.5Bx and add standby powder to mix, massecuite namely obtains nutrient sugar after vacuum drying is cooling.
Detect the quality of embodiment 1 to embodiment 5 gained nutrient sugar by " the brown granulated sugar test method " of QB/T 2343.2-1997 standard, main project and the index of detection are as shown in table 1.
Table 1
Every data in table 1 all meet the QB/T2343.1-1997 standard.
Other main matter content that detects embodiment 1 to embodiment 5 gained nutrient sugar with liquid chromatography, GB/T8313-2008 forint phenol reagent process is as shown in table 2.
Table 2
The present invention can either remove harmful inorganic ash content in the sugaring material, can keep again nutritional labeling useful in material and function of human body be had the material of regulating action, resource is fully utilized and guarantees Environmental security; And prepared nutrient sugar has the distinctive fragrance of sugarcane.
Claims (6)
1. the material of refining sugar is made the method for nutrient sugar, comprise raw material extraction of the juice, sugarcane juice clarification, evaporate, boil sugar, crystallization in motion, purging and drying process, it is characterized in that: boil the honey that sugared back segment material sieves out through crystallization in motion, purging and carry out clarify process described, described honey is that second green molasses, second are washed honey or molasses, and the clear syrup that processing obtains is as the raw material of boiling massecuite; Put into sugar and plant in crystallizing tank, then put into described clear syrup boiling massecuite, described sugar is planted and the volume ratio of boiling massecuite finished product is 1:2 ~ 3; When material concentration in tank when being 104Bx ~ 106Bx boiling complete, emit massecuite, massecuite namely gets required product through vacuum drying;
The step of described clarify process is as follows:
A, dilution: honey is diluted to 60 Bx ~ 70Bx;
B, heating: the honey after dilution is heated to 70 ℃ ~ 80 ℃;
C, floating: the heating honey that compressed air the is passed into step B floating of getting blisters in floating device clears out the foam of floating;
D, sedimentation: form calcium monohydrogen phosphate-calcium phosphate network sedimentation in the honey of having removed foam with calcium hydroxide and the step C of phosphoric acid and 1.0 ~ 1.2 phosphoric acid equivalents, add again the suspended particulate impurity sedimentation in the auxiliary absorption of flocculant honey, obtain clearly syrup as the raw material of boiling massecuite.
2. sugaring material according to claim 1 is made the method for nutrient sugar, it is characterized in that: the precipitum that produces in clarify process step D is carried out centrifugation, and the clear syrup that obtains is as the raw material that boils sugar.
3. sugaring material according to claim 1 and 2 is made the method for nutrient sugar, and it is characterized in that: described phosphoric acid consumption is 800 ppm ~ 2400ppm, and described flocculant consumption is 2.5 ppm ~ 10ppm.
4. sugaring material according to claim 1 and 2 is made the method for nutrient sugar, it is characterized in that: the foam that clears out by floating in clarify process is formed powder through vacuum drying, described powder is added in massecuite.
5. sugaring material according to claim 4 is made the method for nutrient sugar, and it is characterized in that: come the boiling massecuite by the triose cooking technology, brew temperatures is 68 ℃ ~ 73 ℃, and pressure is-0.095Mpa ~-0.105Mpa.
6. sugaring material according to claim 1 is made the method for nutrient sugar, it is characterized in that: the purity that described sugar is planted is 65 Ap ~ 85 Ap, and the hammer degree is for being 80 Bx ~ 83Bx.
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| CN103271265A (en) * | 2013-05-30 | 2013-09-04 | 佐源集团有限公司 | Production process of black soft sugar |
| CN103993106A (en) * | 2014-05-16 | 2014-08-20 | 广西大学 | Industrialized production method of primitive brown sugar |
| CN104012830A (en) * | 2013-11-20 | 2014-09-03 | 柳州市柳冰食品厂 | Production method for block-shaped grosvener siraitia brown sugar |
| CN104195271A (en) * | 2014-09-28 | 2014-12-10 | 桂林正翰科技开发有限责任公司 | Method for producing refined sugar through ion-exchange fiber high efficiency decolorization one-step method |
| CN105153245A (en) * | 2015-09-23 | 2015-12-16 | 河南正弘药用辅料有限公司 | Production technology for medicinal cane sugar |
| CN105192220A (en) * | 2015-05-22 | 2015-12-30 | 舒文一 | Candy and production method thereof |
| CN106119428A (en) * | 2016-08-17 | 2016-11-16 | 施如涛 | A kind of brown sugar (Saccharum Sinensis Roxb.) remelt syrup two step method clarification process |
| CN106148575A (en) * | 2016-08-17 | 2016-11-23 | 施如涛 | A kind of defecation method of brown sugar (Saccharum Sinensis Roxb.) remelt syrup |
| CN108034772A (en) * | 2017-12-18 | 2018-05-15 | 广西农垦糖业集团西江制糖有限公司 | A kind of manufacture method of high-quality brown granulated sugar |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN103271265B (en) * | 2013-05-30 | 2014-10-08 | 佐源集团有限公司 | Production process of black soft sugar |
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| CN104012830A (en) * | 2013-11-20 | 2014-09-03 | 柳州市柳冰食品厂 | Production method for block-shaped grosvener siraitia brown sugar |
| CN103993106A (en) * | 2014-05-16 | 2014-08-20 | 广西大学 | Industrialized production method of primitive brown sugar |
| CN103993106B (en) * | 2014-05-16 | 2015-12-02 | 广西大学 | A kind of ecosystem brown sugar industrial production method |
| CN104195271A (en) * | 2014-09-28 | 2014-12-10 | 桂林正翰科技开发有限责任公司 | Method for producing refined sugar through ion-exchange fiber high efficiency decolorization one-step method |
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| CN105153245A (en) * | 2015-09-23 | 2015-12-16 | 河南正弘药用辅料有限公司 | Production technology for medicinal cane sugar |
| CN105153245B (en) * | 2015-09-23 | 2018-06-15 | 河南正弘药用辅料有限公司 | A kind of production technology of medical cane sugar |
| CN106148575A (en) * | 2016-08-17 | 2016-11-23 | 施如涛 | A kind of defecation method of brown sugar (Saccharum Sinensis Roxb.) remelt syrup |
| CN106119428A (en) * | 2016-08-17 | 2016-11-16 | 施如涛 | A kind of brown sugar (Saccharum Sinensis Roxb.) remelt syrup two step method clarification process |
| CN108034772A (en) * | 2017-12-18 | 2018-05-15 | 广西农垦糖业集团西江制糖有限公司 | A kind of manufacture method of high-quality brown granulated sugar |
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