CN103757143A - Syrup clarification method - Google Patents
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- CN103757143A CN103757143A CN201410011461.9A CN201410011461A CN103757143A CN 103757143 A CN103757143 A CN 103757143A CN 201410011461 A CN201410011461 A CN 201410011461A CN 103757143 A CN103757143 A CN 103757143A
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- 238000005352 clarification Methods 0.000 title claims abstract description 76
- 238000000034 method Methods 0.000 title claims abstract description 58
- 239000006188 syrup Substances 0.000 title claims description 4
- 235000020357 syrup Nutrition 0.000 title claims description 4
- 235000011389 fruit/vegetable juice Nutrition 0.000 claims abstract description 173
- 235000000346 sugar Nutrition 0.000 claims abstract description 166
- 238000005188 flotation Methods 0.000 claims abstract description 37
- 239000012528 membrane Substances 0.000 claims abstract description 34
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims abstract description 30
- 238000000926 separation method Methods 0.000 claims abstract description 26
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims abstract description 15
- 238000001914 filtration Methods 0.000 claims abstract description 14
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims abstract description 12
- 235000011941 Tilia x europaea Nutrition 0.000 claims abstract description 12
- 239000004571 lime Substances 0.000 claims abstract description 12
- 238000010438 heat treatment Methods 0.000 claims abstract description 10
- 235000007201 Saccharum officinarum Nutrition 0.000 claims description 14
- 240000000111 Saccharum officinarum Species 0.000 claims description 14
- 238000007667 floating Methods 0.000 claims description 8
- 210000000416 exudates and transudate Anatomy 0.000 claims description 6
- 238000001704 evaporation Methods 0.000 claims description 5
- 230000008020 evaporation Effects 0.000 claims description 5
- 238000009288 screen filtration Methods 0.000 claims description 5
- 239000008394 flocculating agent Substances 0.000 claims description 3
- 235000016068 Berberis vulgaris Nutrition 0.000 claims description 2
- 241000335053 Beta vulgaris Species 0.000 claims description 2
- 238000006386 neutralization reaction Methods 0.000 claims description 2
- 229920000642 polymer Polymers 0.000 claims description 2
- 239000011148 porous material Substances 0.000 claims description 2
- 238000007670 refining Methods 0.000 claims 1
- 229930006000 Sucrose Natural products 0.000 abstract description 6
- 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
- 230000008878 coupling Effects 0.000 abstract description 5
- 238000010168 coupling process Methods 0.000 abstract description 5
- 238000005859 coupling reaction Methods 0.000 abstract description 5
- 238000005516 engineering process Methods 0.000 abstract description 5
- 239000005720 sucrose Substances 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 description 10
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 238000003958 fumigation Methods 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 235000016709 nutrition Nutrition 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 241000219310 Beta vulgaris subsp. vulgaris Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- CZMRCDWAGMRECN-UHFFFAOYSA-N Rohrzucker Natural products OCC1OC(CO)(OC2OC(CO)C(O)C(O)C2O)C(O)C1O CZMRCDWAGMRECN-UHFFFAOYSA-N 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 235000021536 Sugar beet Nutrition 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 208000012826 adjustment disease Diseases 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 239000008395 clarifying agent Substances 0.000 description 1
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- 238000010586 diagram Methods 0.000 description 1
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- 239000000796 flavoring agent Substances 0.000 description 1
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- 238000005189 flocculation Methods 0.000 description 1
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- 239000006260 foam Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
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- 235000021552 granulated sugar Nutrition 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000007726 management method Methods 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
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- 235000019698 starch Nutrition 0.000 description 1
- 150000008163 sugars Chemical class 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
本发明涉及一种糖汁澄清的方法,属于制糖工业糖汁澄清技术领域。所述糖汁澄清方法是糖汁气浮澄清和膜分离耦合技术对糖汁进行清净,包括糖汁气浮澄清前处理、糖汁气浮澄清、糖汁膜分离系统三道主要工序;首先对糖汁进行气浮澄清前处理,即将糖汁进行滤网过滤、添加石灰、磷酸调整pH值和一级加热处理,处理后糖汁进入气浮澄清系统进行处理,将糖汁中网络的非糖分除去,气浮澄清得到的浮清糖汁首先经过糖汁过滤系统处理,然后进入高效的糖汁膜分离系统中澄清,最终得到澄清质量不低于传统制糖工艺的清糖汁,由此完成糖汁的澄清过程。本发明工艺过程主要采用气浮澄清和膜分离耦合技术,方法简单先进,糖汁停留时间短,蔗糖分损失少,澄清稳定可控,澄清效率高,是糖厂实现节能与清洁生产,实施可持续发展的有效措施,具有较好的应用前景。
The invention relates to a method for clarifying sugar juice, which belongs to the technical field of sugar juice clarification in the sugar industry. The sugar juice clarification method is the sugar juice air flotation clarification and membrane separation coupling technology to clean the sugar juice, including three main processes of sugar juice air flotation clarification pretreatment, sugar juice air flotation clarification, and sugar juice membrane separation system; The sugar juice is pre-treated by air flotation and clarification, that is, the sugar juice is filtered through a filter, lime, phosphoric acid is added to adjust the pH value, and the first-level heat treatment is carried out. The clear sugar juice obtained by air flotation clarification is firstly processed by the sugar juice filtration system, and then enters the high-efficiency sugar juice membrane separation system for clarification, and finally obtains clear sugar juice whose clarification quality is not lower than that of the traditional sugar making process, thus completing The clarification process of sugar juice. The technical process of the present invention mainly adopts air flotation clarification and membrane separation coupling technology, the method is simple and advanced, the residence time of sugar juice is short, the loss of sucrose is small, the clarification is stable and controllable, and the clarification efficiency is high. It is an effective measure for sustainable development and has a good application prospect.
Description
技术领域 technical field
本发明属于利用糖汁气浮澄清和膜分离耦合技术澄清糖汁的方法,糖汁所述的糖汁包括甘蔗初压汁、甘蔗混合汁、甘蔗渗出汁、甜菜渗出汁、中和汁、滤汁、蒸发过程的中间糖汁和浓缩糖浆,用于甘蔗和甜菜制糖中糖汁的澄清,糖汁停留时间短,蔗糖分损失少,澄清稳定可控,澄清效率高,可提高糖汁的清净效果和产品的质量,是糖厂实现清洁生产,实施可持续发展的有效措施,具有较好的应用前景。 The invention belongs to a method for clarifying sugar juice by using air flotation clarification and membrane separation coupling technology. The sugar juice described in the sugar juice includes sugarcane initial press juice, sugarcane mixed juice, sugarcane exudate juice, beet exudate juice, and neutralized juice , intermediate sugar juice and concentrated syrup in the process of filtering juice and evaporation, used for clarification of sugar juice in sugar cane and beet sugar production, the residence time of sugar juice is short, the loss of sucrose is small, the clarification is stable and controllable, the clarification efficiency is high, and the sugar can be improved. The cleaning effect of the juice and the quality of the product are effective measures for the sugar factory to realize clean production and implement sustainable development, and it has a good application prospect.
背景技术 Background technique
在糖厂对混合汁的处理有经典的碳酸法和亚硫酸法澄清工艺,碳酸法由于滤泥排放量大,有机质含量低,碳酸钙含量达80%以上,无农用价值,目前,国内外碳酸法糖厂的滤泥基本上是采用湿排或干排处理,给环境造成了严重的污染,由于碳酸法制糖工艺存在滤泥污染严重问题,许多糖厂选择亚硫酸法澄清工艺,传统亚硫酸法澄清工艺存在硫熏强度高、糖汁澄清效率低、糖汁在沉降器中停留时间长、沉降池操作控制容易反底等问题,这些问题亟待解决。 There are classic carbonation and sulfurous acid clarification processes for the mixed juice in the sugar factory. Due to the large discharge of filter sludge, low organic matter content and calcium carbonate content of more than 80%, the carbonation method has no agricultural value. At present, carbonation at home and abroad The filter mud of French sugar factories is basically treated by wet discharge or dry discharge, which has caused serious pollution to the environment. Due to the serious problem of filter sludge pollution in the carbonic acid sugar production process, many sugar factories choose the sulfurous acid clarification process. The traditional sulfurous acid There are problems such as high sulfur fumigation intensity, low sugar juice clarification efficiency, long residence time of sugar juice in the settler, and easy bottom reversal in the operation and control of the settling tank. These problems need to be solved urgently.
对于传统亚硫酸法澄清工艺的研究一直在进行,如采用半碳法半亚法蔗汁气浮澄清法和低温磷浮糖汁澄清法等工艺探索,能除去制糖生产工艺处理蔗汁中的蔗糠、淀粉、蔗脂、蔗腊、植物色素、蛋白质和胶体等非糖分,有利于后处理效果。中国专利(申请号)201310082816.9公开了一种蔗汁澄清方法,采用部分混合汁制泡浮清分离结合糖汁快速沉降方法澄清糖汁,混合汁依次经预灰、一级加热、制泡、气浮分离、二级加热、硫熏中和、中和汁加热、快速沉降步骤处理得到清汁,能稳定清汁pH 值,避免沉淀池“反底”和“蔗糖转化”现象,节约生产成本,减少环境污染,提高产品质量;中国专利(申请号:201110360967.7)公开了一种多级膜并行生产营养糖、风味蔗汁及饲料原料的方法,该方法采用多级膜过滤用于生产营养糖。 Research on the traditional sulfurous acid clarification process has been going on, such as the use of semi-carbon and semi-sub-method sugarcane juice air flotation clarification and low-temperature phosphorus floating sugar juice clarification, which can remove sugar in sugarcane juice. Cane bran, starch, sucrose fat, sucrose wax, plant pigments, proteins and colloids and other non-sugar components are beneficial to the post-processing effect. Chinese Patent (Application No.) 201310082816.9 discloses a sugarcane juice clarification method, which uses part of the mixed juice to make foam, float and clear the separation combined with the rapid sedimentation method of sugar juice to clarify the sugar juice. Floating separation, secondary heating, sulfur fuming neutralization, neutralizing juice heating, and rapid sedimentation steps to obtain clear juice can stabilize the pH value of clear juice, avoid "bottom inversion" and "sucrose conversion" in sedimentation tanks, save production costs and reduce environmental pollution. Pollution, improve product quality; Chinese patent (application number: 201110360967.7) discloses a method for parallel production of nutritional sugar, flavor cane juice and feed materials with multi-stage membranes. The method uses multi-stage membrane filtration for the production of nutritional sugars.
国外比较先进的糖液澄清方法有离子交换法、膜分离法,离子交换法在国外炼糖厂应用推广较多,国内也引进过先进的离子交换装备,但是存在对处理物料质量要求高、操作复杂、管理要求高等问题,国内炼糖厂未能很好应用与推广,膜分离法由于膜材料、膜衰减问题多,至今也未在工业化大规模白砂糖生产中示范应用。 The more advanced sugar solution clarification methods in foreign countries include ion exchange method and membrane separation method. Ion exchange method is widely used in foreign sugar refineries. Due to the complexity and high management requirements, domestic sugar refineries have not been well applied and promoted. Due to the many problems of membrane materials and membrane attenuation, the membrane separation method has not yet been demonstrated and applied in large-scale industrial white sugar production.
因此,制糖领域迫切需要开发一种能够满足我国耕地白砂糖生产的高效糖汁清净新工艺,来解决这些问题。 Therefore, there is an urgent need to develop a new process for cleaning high-efficiency sugar juice that can meet the requirements of my country's cultivated land white granulated sugar to solve these problems.
发明内容 Contents of the invention
本发明提供了一种糖汁气浮澄清和膜分离耦合技术对糖汁进行清净的方法,能解决传统制糖过程废物污染、清净效率不高、膜通量低、膜使用周期短等技术缺陷,并可获得较高质量的清糖汁。 The invention provides a method for cleaning sugar juice by air flotation clarification and membrane separation coupling technology, which can solve technical defects such as waste pollution, low cleaning efficiency, low membrane flux, and short membrane service life in the traditional sugar production process. , and can obtain higher quality clear sugar juice.
本发明是通过下述的技术方案加以实现的。 The present invention is achieved through the following technical solutions.
一种糖汁澄清方法,包括糖汁气浮澄清前处理、糖汁气浮澄清、糖汁膜分离系统三道主要工序,其特征在于:首先对糖汁进行气浮澄清前处理,即将糖汁进行滤网过滤、添加石灰、磷酸调整pH值和一级加热处理,处理后糖汁进入糖汁气浮澄清系统进行处理,即预处理后糖汁经过再次添加石灰或磷酸调整pH值、全部糖汁或部分糖汁制泡、添加絮凝剂和澄清剂,将糖汁中的非糖分网络除去,气浮澄清处理系统得到的浮清糖汁首先经过糖汁过滤系统处理,然后进入高效的糖汁膜分离系统中澄清,最终得到澄清质量不低于传统制糖工艺的清糖汁,由此完成糖汁的澄清过程。 A sugar juice clarification method, comprising three main processes of sugar juice air flotation clarification pretreatment, sugar juice air flotation clarification, and sugar juice membrane separation system, characterized in that: firstly, the sugar juice is subjected to air flotation clarification pretreatment, that is, the sugar juice Carry out filter screen filtration, add lime, phosphoric acid to adjust the pH value and primary heat treatment. After the treatment, the sugar juice enters the sugar juice air flotation clarification system for treatment, that is, after the pretreatment, the sugar juice is added again to adjust the pH value of lime or phosphoric acid Juice or part of the sugar juice is bubbled, flocculants and clarifiers are added to remove the non-sugar network in the sugar juice, and the floating clear sugar juice obtained by the air flotation clarification treatment system is first processed by the sugar juice filtration system, and then enters the high-efficiency sugar juice Clarify in the membrane separation system, and finally obtain the clear sugar juice whose clarification quality is not lower than that of the traditional sugar making process, thus completing the clarification process of the sugar juice.
所述的糖汁包括甘蔗初压汁、甘蔗混合汁、甘蔗渗出汁、甜菜渗出汁、中和汁、滤汁、蒸发过程的中间糖汁和浓缩糖浆。 The sugar juice includes sugarcane initial press juice, sugarcane mixed juice, sugarcane exudate juice, sugar beet exudate juice, neutralized juice, filtered juice, intermediate sugar juice in the evaporation process and concentrated syrup.
所述的糖汁进行气浮澄清前处理滤网过滤系统的滤网目数为100~800目,添加石灰和磷酸控制pH值在6.0~11.0范围,磷酸值以每公斤糖汁含P2O5毫克数计算在200~450mg范围,一次加热后温度在50~65℃范围。 The sugar juice is subjected to air flotation and clarification pretreatment. The filter mesh of the filter system is 100-800 mesh, adding lime and phosphoric acid to control the pH value in the range of 6.0-11.0, and the phosphoric acid value is P2O per kilogram of sugar juice The number of 5 mg is calculated in the range of 200-450 mg, and the temperature after one heating is in the range of 50-65 °C.
所述的糖汁气浮澄清系统中再次加石灰工艺指标控制是pH值在7.0~8.5范围,糖汁中磷酸总值以每公斤糖汁含P2O5毫克数计算在400~500mg范围,所用的絮凝剂为糖用高分子絮凝剂,絮凝剂用量对糖汁量为2~10ppm,糖用澄清剂用量对糖汁量0.1%~10%。 In the sugar juice air flotation clarification system, the process index control of adding lime again is that the pH value is in the range of 7.0 to 8.5, and the total value of phosphoric acid in the sugar juice is in the range of 400 to 500 mg calculated as 5 mg of P2O per kilogram of sugar juice. The flocculant used is a polymer flocculant for sugar, the amount of flocculant is 2-10ppm to the amount of sugar juice, and the amount of clarifying agent for sugar is 0.1%-10% to the amount of sugar juice.
所述的气浮澄清后糖汁过滤系统的过滤精度在5~40微米范围,糖汁膜分离系统的过滤膜精度在分子量2000~膜孔径2微米范围,滤网过滤系统和膜分离系统适应温度在45~110度范围,处理糖汁锤度在10~78oBx范围。 The filtration precision of the sugar juice filtration system after air flotation clarification is in the range of 5-40 microns, the filtration membrane precision of the sugar juice membrane separation system is in the range of molecular weight 2000 to 2 microns in membrane pore size, and the filter screen filtration system and membrane separation system are suitable for temperature In the range of 45 to 110 degrees, the Brix of the processed sugar juice is in the range of 10 to 78oBx.
所述的糖汁澄清方法得到的清糖汁质量不低于传统制糖澄清方法得到的清糖汁质量。 The quality of the clear sugar juice obtained by the sugar juice clarification method is not lower than that obtained by the traditional sugar clarification method.
本发明具有较强的适应性,对不同地区、不同品种和不同原料的糖汁中非糖成分较大差别的情况下,通过简单调整运行过程中的主要操作参数,即可完成高效澄清,有利于实现自动化控制。与现有的糖汁澄清工艺相比,本发明有利于降低生产能耗,提高产品质量。 The present invention has strong adaptability, and when the non-sugar components in the sugar juice of different regions, different varieties and different raw materials are quite different, the high-efficiency clarification can be completed by simply adjusting the main operating parameters in the operation process, which is effective. Facilitate the realization of automatic control. Compared with the existing sugar juice clarification process, the invention is beneficial to reduce production energy consumption and improve product quality.
与现有技术方案相比,本发明具有以下特点和进步: Compared with prior art solutions, the present invention has the following characteristics and progress:
1、采用低温气浮澄清糖汁,通过两次调整pH值,提高气浮澄清效率,并达到传统蒸发过程对pH值要求,不用再次经过硫熏工艺澄清; 1. Use low-temperature air flotation to clarify sugar juice, adjust the pH value twice, improve the efficiency of air flotation clarification, and meet the pH value requirements of the traditional evaporation process, without having to go through the sulfur fumigation process for clarification again;
2、采用滤网过滤和膜分离方法清净糖汁,可取代传统制糖澄清生产工艺,可提高糖分回收、产品质量和产品的食品安全性,提高膜分离通量,延长膜使用周期。 2. Using filter screen filtration and membrane separation method to clean sugar juice can replace the traditional sugar clarification production process, which can improve sugar recovery, product quality and product food safety, improve membrane separation flux, and prolong membrane service life.
附图Attached picture
图1是本发明的工艺流程图。 Fig. 1 is a process flow diagram of the present invention.
具体实施方式 Detailed ways
下面结合附图,对本发明的具体实施例作进一步详述,但不构成对本发明的任何限制。 The specific embodiments of the present invention will be described in further detail below in conjunction with the accompanying drawings, but this does not constitute any limitation to the present invention.
一种糖汁澄清方法,包括糖汁气浮澄清前处理、糖汁气浮澄清、糖汁膜分离系统三道主要工序,其特征在于:首先对糖汁进行气浮澄清前处理,即将糖汁进行滤网过滤、添加石灰、磷酸调整pH值和一级加热处理,处理后糖汁进入糖汁气浮澄清系统进行处理,即预处理后糖汁经过再次添加石灰调整pH值、全部糖汁或部分糖汁制泡、添加絮凝剂和澄清剂,将糖汁中的非糖分网络除去,气浮澄清处理系统得到的浮清糖汁首先经过糖汁过滤系统处理,然后进入高效的糖汁膜分离系统中澄清,最终得到澄清质量不低于传统制糖工艺的清糖汁,由此完成糖汁的澄清过程。 A sugar juice clarification method, comprising three main processes of sugar juice air flotation clarification pretreatment, sugar juice air flotation clarification, and sugar juice membrane separation system, characterized in that: firstly, the sugar juice is subjected to air flotation clarification pretreatment, that is, the sugar juice Carry out filter screen filtration, add lime, phosphoric acid to adjust the pH value and primary heat treatment. After the treatment, the sugar juice enters the sugar juice air flotation clarification system for treatment, that is, after the pretreatment, the sugar juice is added again to adjust the pH value of the sugar juice, all the sugar juice or Part of the sugar juice is foamed, flocculants and clarifiers are added to remove the non-sugar network in the sugar juice, and the floating clear sugar juice obtained by the air flotation clarification treatment system is first processed by the sugar juice filtration system, and then enters the high-efficiency sugar juice membrane separation Clarify in the system, and finally get the clear sugar juice whose clarification quality is not lower than the traditional sugar making process, thus completing the clarification process of the sugar juice.
所述的糖汁为甘蔗混合汁,锤度在16.5±0.5oBx糖汁进行气浮澄清前处理滤网过滤系统的滤网目数为200目,添加石灰和磷酸控制pH值在8.0±0.2,一次加热后温度在58±0.5℃;糖汁气浮澄清系统中再次加石灰或磷酸工艺指标控制是pH值在7.5±0.1,磷酸总值以每公斤糖汁含P2O5毫克数计算在400±10mg,絮凝剂用量对糖汁量为3ppm,糖用澄清剂用量对糖汁量2±0.2%;滤网过滤系统的过滤精度在10微米,糖汁膜分离系统的过滤精度在0.2微米。 The sugar juice is sugarcane mixed juice, the Brix is 16.5 ± 0.5oBx, the sugar juice is subjected to air flotation clarification pretreatment, the mesh number of the filter screen filter system is 200 mesh, adding lime and phosphoric acid to control the pH value at 8.0 ± 0.2, After the first heating, the temperature is 58±0.5°C; adding lime or phosphoric acid to the sugar juice air flotation clarification system to control the process index is that the pH value is 7.5±0.1, and the total value of phosphoric acid is calculated as 5 mg of P 2 O per kg of sugar juice. 400±10mg, the amount of flocculant to the amount of sugar juice is 3ppm, the amount of sugar clarifier to the amount of sugar juice is 2±0.2%; the filtration accuracy of the filter filter system is 10 microns, and the filtration accuracy of the sugar juice membrane separation system is 0.2 microns .
糖汁澄清工艺为:糖汁首先进行预处理,预处理后的糖汁泵送至糖汁再次pH调整反应箱,随后自流至全汁制泡箱和澄清剂及絮凝反应箱,然后经糖汁气浮澄清池进行澄清处理,浮渣加热至85℃左右冲洗至泥汁箱,浮清糖汁经过曲筛(80目)过滤后流入浮清糖汁箱,浮清糖汁经糖汁输送泵送至滤网过滤系统进行自动过滤,得到的过滤清糖汁经增压泵送至膜分离系统,进行精密清净处理,渗透液即为清净糖汁,经二次加热后送至蒸发系统;浓集液回流至混合汁箱再次进入全汁制泡箱再次气浮处理。 The sugar juice clarification process is as follows: the sugar juice is firstly pretreated, and the pretreated sugar juice is pumped to the sugar juice pH adjustment reaction box again, and then flows to the whole juice foaming box and clarifier and flocculation reaction box, and then passes through the sugar juice The air flotation clarification tank is used for clarification treatment, the scum is heated to about 85°C and washed into the mud tank, the floating sugar juice is filtered through a curved sieve (80 mesh) and then flows into the floating clear sugar juice tank, and the floating clear sugar juice passes through the sugar juice delivery pump Sent to the filter filter system for automatic filtration, the obtained filtered clear sugar juice is sent to the membrane separation system by a booster pump for precise cleaning treatment, the permeate is the clean sugar juice, which is sent to the evaporation system after secondary heating; The collected liquid flows back to the mixed juice box and then enters the whole juice bubble making box for another air flotation treatment.
对此糖厂混合汁进行测定,其混浊度为29886.00 MAU,色值为3157.82 IU,简纯度为81.15;采用传统亚硫酸法处理后,其混浊度为103.56 MAU,色值为1808.34 IU,简纯度为82.46;采用气浮-膜分离法处理后,其混浊度为83.27 MAU,色值为1773.96 IU,简纯度为82.42, 表明经过气浮澄清和膜分离耦合技术澄清的清糖汁质量:清汁与混合汁纯度差和传统方法接近,糖汁混浊度和色值指标均较好,完全达到传统澄清工艺糖汁质量。 The sugar factory mixed juice was measured, the turbidity was 29886.00 MAU, the color value was 3157.82 IU, and the simple purity was 81.15; after the traditional sulfurous acid treatment, the turbidity was 103.56 MAU, the color value was 1808.34 IU, the simple purity After being treated by air flotation-membrane separation method, the turbidity was 83.27 MAU, the color value was 1773.96 IU, and the simple purity was 82.42, indicating the quality of clear sugar juice clarified by air flotation clarification and membrane separation coupling technology: clear juice and The purity difference of the mixed juice is close to that of the traditional method, and the turbidity and color value indicators of the sugar juice are good, which fully meets the quality of the traditional clarification process.
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