CN103060479B - Method for cleaning sugar preparing and boiling materials - Google Patents
Method for cleaning sugar preparing and boiling materials Download PDFInfo
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- CN103060479B CN103060479B CN201310048614.2A CN201310048614A CN103060479B CN 103060479 B CN103060479 B CN 103060479B CN 201310048614 A CN201310048614 A CN 201310048614A CN 103060479 B CN103060479 B CN 103060479B
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- 238000000034 method Methods 0.000 title claims abstract description 53
- 238000009835 boiling Methods 0.000 title claims abstract description 42
- 239000000463 material Substances 0.000 title claims abstract description 31
- 238000004140 cleaning Methods 0.000 title claims abstract 5
- 235000012907 honey Nutrition 0.000 claims abstract description 57
- 238000007667 floating Methods 0.000 claims abstract description 35
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims abstract description 32
- 238000004062 sedimentation Methods 0.000 claims abstract description 32
- 239000006188 syrup Substances 0.000 claims abstract description 24
- 235000020357 syrup Nutrition 0.000 claims abstract description 24
- 239000006260 foam Substances 0.000 claims abstract description 23
- 239000002994 raw material Substances 0.000 claims abstract description 21
- 238000010438 heat treatment Methods 0.000 claims abstract description 20
- 239000012535 impurity Substances 0.000 claims abstract description 17
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims abstract description 16
- 239000002245 particle Substances 0.000 claims abstract description 13
- 239000000920 calcium hydroxide Substances 0.000 claims abstract description 12
- 238000010790 dilution Methods 0.000 claims abstract description 12
- 239000012895 dilution Substances 0.000 claims abstract description 12
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims abstract description 11
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims abstract description 11
- 239000000203 mixture Substances 0.000 claims abstract description 3
- 238000001179 sorption measurement Methods 0.000 claims abstract 2
- 238000003756 stirring Methods 0.000 claims abstract 2
- 235000013379 molasses Nutrition 0.000 claims description 16
- 238000002425 crystallisation Methods 0.000 claims description 15
- 230000008025 crystallization Effects 0.000 claims description 15
- VLCINIKIVYNLPT-UHFFFAOYSA-J dicalcium;hydrogen phosphate Chemical compound [Ca+2].[Ca+2].OP(O)([O-])=O.[O-]P([O-])([O-])=O VLCINIKIVYNLPT-UHFFFAOYSA-J 0.000 claims description 12
- 239000013049 sediment Substances 0.000 claims description 10
- 238000012216 screening Methods 0.000 claims description 2
- 229910019142 PO4 Inorganic materials 0.000 claims 1
- 238000010411 cooking Methods 0.000 claims 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims 1
- 239000010452 phosphate Substances 0.000 claims 1
- 229930006000 Sucrose Natural products 0.000 abstract description 19
- 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 19
- 239000005720 sucrose Substances 0.000 abstract description 18
- 239000002699 waste material Substances 0.000 abstract description 5
- 238000011084 recovery Methods 0.000 abstract description 4
- 238000007664 blowing Methods 0.000 abstract 1
- FUFJGUQYACFECW-UHFFFAOYSA-L calcium hydrogenphosphate Chemical compound [Ca+2].OP([O-])([O-])=O FUFJGUQYACFECW-UHFFFAOYSA-L 0.000 abstract 1
- 239000001506 calcium phosphate Substances 0.000 abstract 1
- 229910000389 calcium phosphate Inorganic materials 0.000 abstract 1
- 235000019700 dicalcium phosphate Nutrition 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 19
- 238000007670 refining Methods 0.000 description 19
- 238000010926 purge Methods 0.000 description 18
- 235000007201 Saccharum officinarum Nutrition 0.000 description 12
- 240000000111 Saccharum officinarum Species 0.000 description 12
- 238000010521 absorption reaction Methods 0.000 description 11
- 239000003795 chemical substances by application Substances 0.000 description 11
- 238000005189 flocculation Methods 0.000 description 11
- 230000016615 flocculation Effects 0.000 description 11
- 235000011116 calcium hydroxide Nutrition 0.000 description 10
- 238000006243 chemical reaction Methods 0.000 description 10
- 238000005119 centrifugation Methods 0.000 description 9
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 9
- 238000005352 clarification Methods 0.000 description 8
- 239000011229 interlayer Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 238000001035 drying Methods 0.000 description 7
- 238000001704 evaporation Methods 0.000 description 7
- 230000008020 evaporation Effects 0.000 description 7
- 238000009923 sugaring Methods 0.000 description 6
- 150000003641 trioses Chemical class 0.000 description 6
- 150000002016 disaccharides Chemical class 0.000 description 5
- 235000009508 confectionery Nutrition 0.000 description 3
- 229920002401 polyacrylamide Polymers 0.000 description 3
- -1 2AP biose Chemical class 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- BJHIKXHVCXFQLS-UYFOZJQFSA-N keto-D-fructose Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)C(=O)CO BJHIKXHVCXFQLS-UYFOZJQFSA-N 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000002269 spontaneous effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Chemical compound OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 229920002527 Glycogen Polymers 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229940096919 glycogen Drugs 0.000 description 1
- 159000000003 magnesium salts Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000001814 pectin Substances 0.000 description 1
- 229920001277 pectin Polymers 0.000 description 1
- 235000010987 pectin Nutrition 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 150000003445 sucroses Chemical class 0.000 description 1
Landscapes
- Jellies, Jams, And Syrups (AREA)
Abstract
本发明公开了一种制糖煮糖物料清净处理的方法，涉及制糖技术领域，其步骤如下：将三系煮糖工序中煮制得到的糖膏经助晶、分蜜筛分出来的蜜进行稀释；把稀释后的蜜加热；通入压缩空气打泡上浮，清出上浮的泡沫；用磷酸和1.0~1.2磷酸当量的氢氧化钙搅拌混合反应与清除了泡沫的蜜中形成磷酸氢钙-磷酸钙网络沉降，再加入絮凝剂辅助吸附蜜中的悬浮颗粒杂质沉降，得到清糖浆作为煮糖的原料。本发明相比较于现有技术，经清净处理的物料纯度提高、粘度降低大部分能够回煮，减少后段物料煮制量，降低废蜜产率，提高蔗糖分收回；纯度提高，粘度降低，蔗糖易结晶吸收，提高蔗糖分收回；大幅度降低废蜜中的无机灰分杂质，提升废蜜使用价值。The invention discloses a method for cleaning and treating sugar-making and boiling-sugar materials, and relates to the technical field of sugar-making. Dilution; heating the diluted honey; blowing compressed air into it to make bubbles and float up, clear out the floating foam; stir and mix with phosphoric acid and 1.0~1.2 calcium hydroxide equivalent of phosphoric acid to form calcium hydrogen phosphate in the honey that has removed the foam -Calcium phosphate network sedimentation, and then add flocculant to assist in the adsorption of suspended particles in the honey to settle, to obtain clear syrup as the raw material for boiling sugar. Compared with the prior art, the present invention improves the purity of the cleaned material and reduces the viscosity, most of which can be boiled back, reduces the amount of material cooked in the later stage, reduces the yield of waste honey, and improves the recovery of sucrose; the purity is improved, the viscosity is reduced, Sucrose is easy to crystallize and absorb, which improves the recovery of sucrose; greatly reduces the inorganic ash impurities in waste honey, and improves the use value of waste honey.
Description
Technical field
The present invention relates to sugar refining field, the method that sugared material is boiled in especially a kind of processing that improves sugaring raw material sugar recovery.
Background technology
In the production process of sugar refinery, it is to boil sugar, crystallization in motion, purging and drying process that the sugar refining technology of white sugar generally comprises raw material extraction of the juice, clarification, evaporation, three, wherein, three is that high-grade massecuite, intermediate massecuite and the raw massecuite obtaining in Boiling Process sieves out honey, commerieal sugar through crystallization in motion, purging respectively, screening sweet purity is out not high, for not affecting quality product, the general honey time of only part first being washed boils high-grade massecuite, another part is as the material of back segment massecuite boiling, make to move after material, reduced the withdrawal of sugar.The purity of sugaring material is higher, and Sucrose is higher, and impurity is fewer, and the easier crystallization of sucrose absorbs, and the recovery of Sucrose is just higher.And current sugar refining technology only carries out clarify process and improves feed purity boiling glycogen material before being Boiling Process three.Existing sugar refining technology material clarify process includes and after raw material extraction of the juice, carries out clarifying treatment, to the clear juice processing of floating after clarification, and the processing of floating of the syrup after evaporization process.Due to factor impacts such as raw material " non-sucrose " impurity component and number change, physical and chemical properties change, existing way are unstable, production operation fluctuation, the purification effect limit, make a large amount of " non-sucrose " impurity fail to remove and enter Boiling Process.These " non-sucrose " impurity one are to hinder sucrose molecules crystallization, regain low; The 2nd, increase material viscosity, regain low; The 3rd, massecuite, molasses are swollen cause to emit case or molasses spontaneous combustion; The 4th, in molasses, inorganic ash content content is too high, has significantly reduced utility value, brings serious potential safety hazard to environment simultaneously.
Summary of the invention
The object of this invention is to provide a kind of sugaring and boil the method for sugared material clarify process, this method can solve existing sugar refining technology and boil the large and sugar of the foreign matter content of sugared material and regain low problem.
In order to address the above problem, the technical solution used in the present invention is: the method for sugared material clarify process is boiled in this sugaring, and its step is as follows:
A, dilution: be that the honey that massecuite that in Boiling Process, boiling obtains sieves out through crystallization in motion, purging dilutes by three, be diluted to 60 Bx ~ 70Bx;
B, heating: the honey after dilution is heated to 70 ℃ ~ 80 ℃;
C, floating: the heating honey that pressurized air is passed into the step B floating of getting blisters in floating device, clears out the foam of floating;
D, sedimentation: be uniformly mixed reaction with the calcium hydroxide of phosphoric acid and 1.0 ~ 1.2 phosphoric acid equivalents and removed in the honey of foam and formed the sedimentation of secondary calcium phosphate-calcium phosphate network with step C, add again the suspended particle impurity sedimentation in the auxiliary absorption of flocculation agent honey, obtain clearly syrup as boiling sugared raw material.
Above-mentioned sugaring is boiled in the technical scheme of method of sugared material clarify process, and technical scheme can also be more specifically: the sediment producing in step D is carried out to centrifugation, and the clear syrup obtaining is as boiling sugared raw material.
Further, described phosphoric acid consumption is 400 ppm ~ 2400ppm, and described flocculation agent consumption is 1.5 ppm ~ 10ppm.
Further, described honey is that high green syrup, first are washed honey, second green molasses, second and washed a kind of in honey, molasses or wherein several.
Preferably, flocculation agent is polyacrylamide.
The principle of technical scheme of the present invention is three to be the high-grade massecuite boiling in sugar, intermediate massecuite, raw massecuite is through boiling, crystallization in motion, purging honey is out separated out after a large amount of Sucroses because of it, " non-sucrose " impurity moiety is stable, physico-chemical property is stable, calcium sulfate, Calucium Silicate powder, magnesium salts etc. are at 60 Bx ~ 70Bx, in the liquid glucose of 70 ℃ ~ 80 ℃, solubility product declines, the characteristic that the overwhelming majority exists with suspended particle, material is removed organic surface-active substance (foam) through floating, add again the compound sediment of secondary calcium phosphate-calcium phosphate that phosphoric acid and milk of lime reaction generate, under flocculation agent booster action, form network sedimentation absorption catch material in suspended state particle inorganic, organic " non-sucrose " impurity.
Owing to having adopted technique scheme, the present invention compared with prior art has following beneficial effect:
1, process by floating, can effectively remove surfactant class " non-sucrose " organic impuritys such as phospholipoprotein mixture, pectin, composite gel, reduce the crystallization of sucrose factor that hinders, reduce material viscosity, improve feed purity, regain thereby improve Sucrose;
2, eliminate intermediate massecuite, raw massecuite, waste molasses swell problem and waste molasses spontaneous combustion problem;
3, add secondary calcium phosphate-calcium phosphate and be aided with the absorption of flocculation agent effect formation network, sedimentation, centrifugation, can effectively remove the inorganic ash content in material, reduce the crystallization of sucrose factor that hinders, improve feed purity, improve Sucrose withdrawal;
4, improve 8 AP ~ 13AP through the feed purity of clarify process, major part can be returned and be boiled, and has reduced back segment material boiling amount, improves Sucrose and regains, and reduces molasses productive rate;
5, in the molasses after clarify process, inorganic ash content content is extremely low, promotes the utility value of molasses.
Embodiment
Embodiment 1
The present embodiment to be to adopt sugarcane as the common sulfurous method sugar refining technology of raw material is 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: by three be high-grade massecuite that in Boiling Process, boiling obtains through purging sieve out high green syrup, first is washed honey and is mixed, the mixing that is 73.5AP the purity being mixed to form honey stream adds in the interlayer steam heating thinning tank of 40 cubic metres, be diluted to 64.5Bx with 65 ℃ of sugar refining technology water, again with steam dilution close be heated to 70 ~ 72 ℃ flow into floating devices, pass into the floating of getting blisters in the honey of heating with pressurized air, clear out the foam of floating; The honey of having removed foam is added in accelerated clarifier, add accelerated clarifier reaction to form the sedimentation of secondary calcium phosphate-calcium phosphate network with 400ppm phosphoric acid and 450ppm calcium hydroxide simultaneously, and adding the auxiliary absorption of 1.5ppm polyacrylamide flocculant suspended particle impurity sedimentation to stream in accelerated clarifier, the purity obtaining after sedimentation is that the clear syrup of 82.3AP returns and boils methose; The sediment that accelerated clarifier is discharged carries out centrifugation with tripod pendulum type batch centrifugal, and the clear syrup that obtains purity and be 82.5AP returns and boils methose.
Embodiment 2
The present embodiment to be to adopt sugarcane as the common sulfurous method sugar refining technology of raw material is 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: be that high green syrup stream that purity that high-grade massecuite that in Boiling Process, boiling obtains sieves out through purging is 67.6AP adds in the interlayer steam heating thinning tank of 40 cubic metres by three, be diluted to 63.5Bx with 65 ℃ of sugar refining technology water, with steam, the honey of dilution is heated to 74 ~ 76 ℃ again and flows into floating device, pass into the floating of getting blisters in the honey of heating with pressurized air, clear out the foam of floating; The honey of having removed foam is added in accelerated clarifier, add accelerated clarifier reaction to form the sedimentation of secondary calcium phosphate-calcium phosphate network with 800ppm phosphoric acid and 950ppm calcium hydroxide simultaneously, and adding the auxiliary absorption of 3.5ppm flocculation agent suspended particle impurity sedimentation to stream in accelerated clarifier, the purity obtaining after sedimentation is the clear syrup boiling of 78.2AP biose; The sediment that accelerated clarifier is discharged carries out centrifugation with tripod pendulum type batch centrifugal, and obtaining purity is the clear syrup boiling biose of 78.5AP.
Embodiment 3
The present embodiment to be to adopt sugarcane as the common sulfurous method sugar refining technology of raw material is 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: be that second that purity that intermediate massecuite that in Boiling Process, boiling obtains sieves out through purging is 49.5AP is washed in the interlayer steam heating thinning tank that sweet stream adds 40 cubic metres by three, be diluted to 63.0Bx with 65 ℃ of sugar refining technology water, with steam, the honey of dilution is heated to 78 ~ 80 ℃ again and flows into floating device, pass into the floating of getting blisters in the honey of heating with pressurized air, clear out the foam of floating; The honey of having removed foam is added in accelerated clarifier, add accelerated clarifier reaction to form the sedimentation of secondary calcium phosphate-calcium phosphate network with 1500ppm phosphoric acid and 1800ppm calcium hydroxide simultaneously, and adding the auxiliary absorption of 5ppm flocculation agent suspended particle impurity sedimentation to stream in accelerated clarifier, the purity obtaining after sedimentation is that the clear syrup of 61.3AP returns and boils biose; The sediment that accelerated clarifier is discharged carries out centrifugation with tripod pendulum type batch centrifugal, and the clear syrup that obtains purity and be 61.7AP returns and boils biose.
Embodiment 4
The present embodiment to be to adopt sugarcane as the common sulfurous method sugar refining technology of raw material is 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: be that second green molasses stream that purity that intermediate massecuite that in Boiling Process, boiling obtains sieves out through purging is 43.5AP adds in the interlayer steam heating thinning tank of 40 cubic metres by three, be diluted to 63.0Bx with 65 ℃ of sugar refining technology water, with steam, the honey of dilution is heated to 76 ~ 78 ℃ again and flows into floating device, pass into the floating of getting blisters in the honey of heating with pressurized air, clear out the foam of floating; The honey of having removed foam is added in accelerated clarifier, add accelerated clarifier reaction to form the sedimentation of secondary calcium phosphate-calcium phosphate network with 2000ppm phosphoric acid and 2200ppm calcium hydroxide simultaneously, and adding the auxiliary absorption of 8ppm flocculation agent suspended particle impurity sedimentation to stream in accelerated clarifier, the purity obtaining after sedimentation is the clear syrup boiling of 55.3AP triose; The sediment that accelerated clarifier is discharged carries out centrifugation with tripod pendulum type batch centrifugal, and obtaining purity is the clear syrup boiling triose of 55.8AP.
Embodiment 5
The present embodiment to be to adopt sugarcane as the common sulfurous method sugar refining technology of raw material is 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: be that molasses stream that purity that raw massecuite that in Boiling Process, boiling obtains sieves out through purging is 33.5AP adds in the interlayer steam heating thinning tank of 40 cubic metres by three, be diluted to 62.5Bx with 65 ℃ of sugar refining technology water, with steam, the honey of dilution is heated to 76 ~ 78 ℃ again and flows into floating device, pass into the floating of getting blisters in the honey of heating with pressurized air, clear out the foam of floating; The honey of having removed foam is added in accelerated clarifier, add accelerated clarifier reaction to form the sedimentation of secondary calcium phosphate-calcium phosphate network with 2400ppm phosphoric acid and 2400ppm calcium hydroxide simultaneously, and adding the auxiliary absorption of 10ppm polyacrylamide flocculant suspended particle impurity sedimentation to stream in accelerated clarifier, the purity obtaining after sedimentation is that the clear syrup of 45.8AP returns and boils triose; The sediment that accelerated clarifier is discharged carries out centrifugation with tripod pendulum type batch centrifugal, and the clear syrup that obtains purity and be 46.2AP returns and boils triose.
Embodiment 6
The present embodiment to be to adopt sugarcane as the common sulfurous method sugar refining technology of raw material is 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: be that second that purity that intermediate massecuite that in Boiling Process, boiling obtains sieves out through purging is 50.3AP is washed in the interlayer steam heating thinning tank that sweet stream adds 40 cubic metres by three, be diluted to 70.0Bx with 65 ℃ of sugar refining technology water, with steam, the honey of dilution is heated to 78 ~ 80 ℃ again and flows into floating device, pass into the floating of getting blisters in the honey of heating with pressurized air, clear out the foam of floating; The honey of having removed foam is added in accelerated clarifier, add accelerated clarifier reaction to form the sedimentation of secondary calcium phosphate-calcium phosphate network with 1400ppm phosphoric acid and 1500ppm calcium hydroxide simultaneously, and adding the auxiliary absorption of 6ppm flocculation agent suspended particle impurity sedimentation to stream in accelerated clarifier, the purity obtaining after sedimentation is that the clear syrup of 62.3AP returns and boils biose; The sediment that accelerated clarifier is discharged carries out centrifugation with tripod pendulum type batch centrifugal, and the clear syrup that obtains purity and be 62.5AP returns and boils biose.The purity that intermediate massecuite is sieved out through purging is that the second green molasses stream of 45.2AP adds in the interlayer steam heating thinning tank of 40 cubic metres, be diluted to 64.0Bx with 65 ℃ of sugar refining technology water, with steam, the honey of dilution is heated to 76 ~ 78 ℃ again and flows into floating device, pass into the floating of getting blisters in the honey of heating with pressurized air, clear out the foam of floating; The honey of having removed foam is added in accelerated clarifier, add accelerated clarifier reaction to form the sedimentation of secondary calcium phosphate-calcium phosphate network with 1800ppm phosphoric acid and 1900ppm calcium hydroxide simultaneously, and adding the auxiliary absorption of 7.5ppm flocculation agent suspended particle impurity sedimentation to stream in accelerated clarifier, the purity obtaining after sedimentation is the clear syrup boiling of 58.0AP triose.The purity that raw massecuite is sieved out through purging is that the molasses stream of 32.0AP adds in the interlayer steam heating thinning tank of 40 cubic metres, be diluted to 60.0Bx with 65 ℃ of sugar refining technology water, with steam, the honey of dilution is heated to 76 ~ 78 ℃ again and flows into floating device, pass into the floating of getting blisters in the honey of heating with pressurized air, clear out the foam of floating; The honey of having removed foam is added in accelerated clarifier, add accelerated clarifier reaction to form the sedimentation of secondary calcium phosphate-calcium phosphate network with 2200ppm phosphoric acid and 2400ppm calcium hydroxide simultaneously, and adding the auxiliary absorption of 10ppm flocculation agent suspended particle impurity sedimentation to stream in accelerated clarifier, the purity obtaining after sedimentation is that the clear syrup of 44.7AP returns and boils triose; The sediment that accelerated clarifier is discharged carries out centrifugation with tripod pendulum type batch centrifugal, and the clear syrup that obtains purity and be 45.0AP returns and boils triose.
Claims (5)
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| CN201310048614.2A CN103060479B (en) | 2013-02-07 | 2013-02-07 | Method for cleaning sugar preparing and boiling materials |
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| CN106148577A (en) * | 2016-08-17 | 2016-11-23 | 施如涛 | A kind of brown granulated sugar dissolved by a-wash prepares the method for high-grade massecuite |
| CN108315501A (en) * | 2017-12-12 | 2018-07-24 | 白教法 | A kind of cane sugar manufacture clarifies new process without sulphur |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102021250A (en) * | 2010-12-02 | 2011-04-20 | 杨鲁昆 | Method for producing high-quality white granulated sugar by clarifying syrup |
| CN102633896A (en) * | 2012-04-23 | 2012-08-15 | 成都欧林生物科技股份有限公司 | Hib polysaccharide purifying technology |
| CN102719568A (en) * | 2012-05-14 | 2012-10-10 | 广西华蓝设计(集团)有限公司 | Cane juice clearing method and equipment |
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Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102021250A (en) * | 2010-12-02 | 2011-04-20 | 杨鲁昆 | Method for producing high-quality white granulated sugar by clarifying syrup |
| CN102633896A (en) * | 2012-04-23 | 2012-08-15 | 成都欧林生物科技股份有限公司 | Hib polysaccharide purifying technology |
| CN102719568A (en) * | 2012-05-14 | 2012-10-10 | 广西华蓝设计(集团)有限公司 | Cane juice clearing method and equipment |
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