CN1629320A - A New Cleaning Technology of Sugar Cane Juice - Google Patents
A New Cleaning Technology of Sugar Cane Juice Download PDFInfo
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- CN1629320A CN1629320A CN 200310121114 CN200310121114A CN1629320A CN 1629320 A CN1629320 A CN 1629320A CN 200310121114 CN200310121114 CN 200310121114 CN 200310121114 A CN200310121114 A CN 200310121114A CN 1629320 A CN1629320 A CN 1629320A
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- sugar
- juice
- temperature
- decolorization
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- 235000011389 fruit/vegetable juice Nutrition 0.000 title claims abstract description 24
- 238000004140 cleaning Methods 0.000 title claims abstract description 5
- 238000000034 method Methods 0.000 claims abstract description 33
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 18
- 235000007201 Saccharum officinarum Nutrition 0.000 claims abstract description 15
- 240000000111 Saccharum officinarum Species 0.000 claims abstract description 15
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract description 12
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 9
- 238000007667 floating Methods 0.000 claims abstract description 6
- 229910052698 phosphorus Inorganic materials 0.000 claims description 10
- 239000011574 phosphorus Substances 0.000 claims description 10
- 238000004042 decolorization Methods 0.000 claims description 8
- 229930006000 Sucrose Natural products 0.000 claims description 5
- 238000004061 bleaching Methods 0.000 claims description 5
- 239000010802 sludge Substances 0.000 claims description 5
- 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 claims description 4
- 239000005720 sucrose Substances 0.000 claims description 4
- 125000000185 sucrose group Chemical group 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 9
- 239000003337 fertilizer Substances 0.000 abstract description 6
- 239000005909 Kieselgur Substances 0.000 abstract description 3
- 230000007935 neutral effect Effects 0.000 abstract description 3
- 238000001914 filtration Methods 0.000 abstract 1
- 238000007873 sieving Methods 0.000 abstract 1
- 239000000049 pigment Substances 0.000 description 7
- 239000000047 product Substances 0.000 description 7
- 239000004568 cement Substances 0.000 description 5
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical group OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 3
- 238000005188 flotation Methods 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 239000000920 calcium hydroxide Substances 0.000 description 2
- 235000011116 calcium hydroxide Nutrition 0.000 description 2
- 238000005352 clarification Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 125000005586 carbonic acid group Chemical group 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
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- Fertilizers (AREA)
Abstract
Description
技术领域technical field
本发明是一种以甘蔗制糖蔗汁的清净工艺,属于清洁生产工艺范畴。The invention relates to a clean process for producing sugar cane juice from sugarcane, which belongs to the category of clean production process.
技术背景technical background
我国甘蔗制糖工业长期以来都是采用传统的生产方法:一种是碳酸法,另一种是亚硫酸法。碳酸法生产工艺生产的糖产品质量较好,但工艺复杂,成本较高,滤泥产生量大。每入榨1万吨甘蔗,产生800吨滤泥。滤泥呈强碱性,不能用作肥料。碱性滤泥中有机质含量高(约11-13%),不能直接用来烧制水泥,需堆存5年以上方可烧制水泥,所以需要建大面积堆场。另外,堆存过程中产生二次污染。目前仍无经济有效的处理碱性滤泥的办法。为了去除非糖份和色素,碳酸法生产过程中需要加入石灰乳,进行两次碳酸饱充,由此导致工艺流程加长。糖厂三分之一的投资即为达此目的。亚硫酸法生产工艺较简单,投资较少,且滤泥可以作为农田肥料,所以大多数采用该法。但是其产品质量不如碳酸法,产品色值、浊度、灰份、含硫量高,容易返黄,保存性差,日益不符合市场需要。出于国际竞争需要,从2002/2003榨季起,国家将白砂糖的产品质量标准中白砂糖SO2含量从40mg/kg调整为30mg/kg,并且要求逐年降低,计划于2005年白砂糖SO2含量指标要降至10mg/kg以下。可见国家对糖产品质量要求越来越严格,亚硫酸法糖产品的质量问题直接影响到其生存。my country's sugarcane sugar industry has long adopted traditional production methods: one is carbonic acid and the other is sulfurous acid. The quality of sugar products produced by the carbonic acid production process is good, but the process is complicated, the cost is high, and the amount of filter mud is large. For every 10,000 tons of sugarcane squeezed, 800 tons of filter mud are produced. The filter mud is strongly alkaline and cannot be used as a fertilizer. Alkaline filter mud has a high content of organic matter (about 11-13%) and cannot be directly used to burn cement. It needs to be stored for more than 5 years before burning cement, so it is necessary to build a large area of storage yard. In addition, secondary pollution is generated during the storage process. At present, there is still no economical and effective way to deal with alkaline filter sludge. In order to remove non-sugar and pigment, milk of lime needs to be added in the production process of carbonation, and carbonation is carried out twice, which leads to lengthening of the process flow. One-third of the investment in sugar factories is for this purpose. The production process of sulfite method is relatively simple, the investment is less, and the filter mud can be used as farmland fertilizer, so most of them adopt this method. But its product quality is not as good as carbonic acid method, and product color value, turbidity, ash content, sulfur content are high, easy to turn yellow, and preservation is poor, increasingly does not meet market demand. Due to the needs of international competition, starting from the 2002/2003 crushing season, the state adjusted the SO 2 content of white sugar in the product quality standard from 40mg/kg to 30mg/kg, and the requirement was reduced year by year. 2 The content index should be reduced to below 10mg/kg. It can be seen that the country has more and more strict requirements on the quality of sugar products, and the quality problems of sulfite sugar products directly affect their survival.
目前国内正在研究开发低温磷浮法—碳酸法澄清工艺。该工艺在碳酸饱充前,先进行低温磷浮处理,除去大部分有机非糖份。浮清汁的纯度明显上升,胶体和色素大大减少,大大减轻了澄清处理的负担。低温磷浮后再进行碳酸饱充,所需的加灰量大大减少。该工艺把滤泥分为两种,一种含有丰富的有机非糖份以及氮磷钾等肥效的中性滤泥,可以直接用作肥料;另一种含有很少的有机非糖份,碳酸钙含量高达85%以上的碱性滤泥,可以直接烧制水泥或作其它的工业使用,并且由于加灰量大大减少而有效减少了碱性滤泥的产生量。但是该工艺仍存在以下主要问题:(1)碱性滤泥直接烧制水泥,成本较高,难于为水泥生产厂家所接受;(2)低温磷浮法的采用,导致糖产品成本有所提高;(3)该工艺较传统碳酸法工艺长。At present, China is researching and developing low-temperature phosphorus floatation-carbonic acid clarification process. In this process, before carbonation, low-temperature phosphorus flotation treatment is carried out to remove most of the organic non-sugar content. The purity of the supernatant juice is obviously increased, and the colloid and pigment are greatly reduced, which greatly reduces the burden of clarification treatment. After low-temperature phosphorus flotation, carbonation is carried out, and the amount of ash required is greatly reduced. The process divides the filter mud into two types, one is rich in organic non-sugar and neutral filter mud with nitrogen, phosphorus and potassium fertilizer effects, which can be directly used as fertilizer; the other contains very little organic non-sugar, carbonic acid The alkaline filter mud with a calcium content of more than 85% can be directly fired into cement or used in other industries, and the production of alkaline filter mud is effectively reduced due to the greatly reduced amount of ash added. But this process still has the following main problems: (1) the direct firing of cement with alkaline filter mud is costly and difficult to be accepted by cement manufacturers; ; (3) The process is longer than the traditional carbonation process.
发明内容Contents of the invention
本发明的目的是提供一种甘蔗制糖蔗汁清净的清洁生产工艺,即甘蔗制糖混合汁先经低温磷浮法处理,去除非糖份和部分色素,然后利用硅藻土和活性炭作吸附脱色剂,进一步去除浮清汁中的色素,使之达到煮糖的要求。该工艺不产生碱性滤泥。The purpose of the present invention is to provide a clean production process for sugarcane juice, that is, the sugarcane mixed juice is first treated with low-temperature phosphorus floatation to remove non-sugar and part of the pigment, and then use diatomite and activated carbon for adsorption Decolorizing agent, to further remove the pigment in the floating clear juice, so that it can meet the requirements of boiling sugar. This process does not produce alkaline filter sludge.
本发明的目的是通过如下技术方案实现的:The purpose of the present invention is achieved through the following technical solutions:
一种甘蔗制糖蔗汁清净工艺,其工艺流程为:甘蔗制糖混合汁先经低温磷浮法处理,去除非糖份和部分色素;然后采用硅藻土对浮清汁预脱色,预脱色后的糖汁采用活性炭进一步脱色,再送去煮糖(详见本发明工艺流程图)。A process for cleaning sugarcane juice from sugar cane. The process flow is as follows: the mixed sugar cane juice is first treated with low-temperature phosphorus floatation to remove non-sugar and part of the pigment; The sugar juice adopts gac to further decolorize, and then sends to boil sugar (see process flow chart of the present invention for details).
本发明提供的工艺流程的特点在于:The technical process provided by the invention is characterized in that:
采用低温磷浮法与浮清汁吸附脱色联合的蔗汁清净新工艺,避免了碳酸法、低温磷浮法-碳酸法所造成的碱性滤泥,缩短了工艺流程。The new sugarcane juice cleaning process combined with low-temperature phosphorus flotation and floating clear juice adsorption and decolorization avoids the alkaline filter sludge caused by the carbonation method and low-temperature phosphorus flotation-carbonation method, and shortens the process flow.
采用低温磷浮法处理甘蔗压榨混合汁,去除非糖份,同时去除了部分色素,从而提高了糖汁纯度,降低了其色值。The low-temperature phosphorous floatation method is used to treat the mixed sugarcane squeezed juice to remove non-sugar and part of the pigment, thereby improving the purity of the sugar juice and reducing its color value.
采用硅藻土和活性炭作吸附脱色剂,进一步去除浮清汁中的色素,保证处理后的糖汁满足煮糖的要求。Diatomaceous earth and activated carbon are used as adsorption decolorizers to further remove the pigment in the floating clear juice to ensure that the processed sugar juice meets the requirements for boiling sugar.
硅藻土预脱色过程中,硅藻土在800℃焙烧6h后使用,其加入量为蔗糖份的1-3wt.%,预脱色温度为50-75℃,预脱色时间为30-60min。In the diatomite pre-bleaching process, the diatomite is used after roasting at 800° C. for 6 hours, the amount added is 1-3 wt.% of sucrose, the pre-bleaching temperature is 50-75° C., and the pre-bleaching time is 30-60 minutes.
活性炭脱色过程中,活性炭加入量为蔗糖份的0.6-1.5wt.%,脱色温度为50-85℃,脱色时间为15-90min。During the decolorization process of the activated carbon, the dosage of the activated carbon is 0.6-1.5wt.% of the sucrose, the decolorization temperature is 50-85°C, and the decolorization time is 15-90min.
实施例Example
纯度为78.19AP的混合汁,预热至50℃,加入磷酸混合剂,用石灰乳中和,充入微细均匀的气泡,并加入絮凝剂,进行低温磷浮法处理。分离后的中性滤泥可以直接用作肥料或进一步提取高附加值产品。清汁纯度提高到80.66AP,色值降至92.66°st。将浮清汁加热到75℃,加入相对于蔗糖份1.0wt.%的硅藻土,预脱色60min,糖汁色值降至75.23°st。然后加入相对于蔗糖份1.0wt.%的糖用活性炭,继续脱色30min,糖汁色值降至30.70°st,可以满足煮糖的要求。该过程不产生碱性滤泥。For mixed juice with a purity of 78.19AP, preheat to 50°C, add phosphoric acid mixture, neutralize with milk of lime, fill in fine and uniform bubbles, add flocculant, and perform low-temperature phosphorus floatation treatment. The separated neutral filter mud can be directly used as fertilizer or further extracted with high value-added products. The purity of clear juice increased to 80.66AP, and the color value decreased to 92.66°st. Heat the supernatant juice to 75°C, add 1.0wt.% diatomaceous earth relative to the sucrose, pre-decolorize for 60min, and the color value of the juice drops to 75.23°st. Then add 1.0wt.% activated carbon for sugar relative to the sucrose part, continue to decolorize for 30min, and the color value of the juice drops to 30.70 ° st, which can meet the requirements of boiling sugar. This process does not produce alkaline filter sludge.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200310121114 CN1629320A (en) | 2003-12-15 | 2003-12-15 | A New Cleaning Technology of Sugar Cane Juice |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200310121114 CN1629320A (en) | 2003-12-15 | 2003-12-15 | A New Cleaning Technology of Sugar Cane Juice |
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| Publication Number | Publication Date |
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| CN1629320A true CN1629320A (en) | 2005-06-22 |
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| CN 200310121114 Pending CN1629320A (en) | 2003-12-15 | 2003-12-15 | A New Cleaning Technology of Sugar Cane Juice |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100519764C (en) * | 2006-10-27 | 2009-07-29 | 云南永德糖业集团有限公司 | Method for improving sufurous-acid sugar producing process by using suger-used high efficiency active carbon |
| CN102725425A (en) * | 2009-11-11 | 2012-10-10 | 卡博Ua有限公司 | Compositions and methods for improved carbonation clarification of sugar liquors and syrups |
| CN102906279A (en) * | 2009-12-23 | 2013-01-30 | 卡博Ua有限公司 | Compositions and processes for clarification of sugar juices and syrups |
| CN103007624A (en) * | 2012-12-16 | 2013-04-03 | 西王药业有限公司 | Decolorizing active carbon recycle device and production technique |
| CN103210095A (en) * | 2009-11-11 | 2013-07-17 | 卡博Ua有限公司 | Compositions and processes for improving phosphatation clarification of sugar liquors and syrups |
| US9175358B2 (en) | 2009-11-11 | 2015-11-03 | Carbo-UA Limited | Compositions and processes for sugar treatment |
| CN105238883A (en) * | 2015-10-27 | 2016-01-13 | 广西大学 | Purification and decoloring method of cane molasses |
| CN106319098A (en) * | 2016-09-26 | 2017-01-11 | 广西科技大学 | Sugar juice decoloring agent and sugar juice purification decoloring method |
| CN110305989A (en) * | 2019-07-08 | 2019-10-08 | 广西壮族自治区亚热带作物研究所(广西亚热带农产品加工研究所) | A kind of preparation method of mango brown sugar |
-
2003
- 2003-12-15 CN CN 200310121114 patent/CN1629320A/en active Pending
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100519764C (en) * | 2006-10-27 | 2009-07-29 | 云南永德糖业集团有限公司 | Method for improving sufurous-acid sugar producing process by using suger-used high efficiency active carbon |
| CN102725425A (en) * | 2009-11-11 | 2012-10-10 | 卡博Ua有限公司 | Compositions and methods for improved carbonation clarification of sugar liquors and syrups |
| CN103210095A (en) * | 2009-11-11 | 2013-07-17 | 卡博Ua有限公司 | Compositions and processes for improving phosphatation clarification of sugar liquors and syrups |
| US9163293B2 (en) | 2009-11-11 | 2015-10-20 | Carbo-UA Limited | Compositions and processes for improving phosphatation clarification of sugar liquors and syrups |
| US9163292B2 (en) | 2009-11-11 | 2015-10-20 | Carbo-UA Limited | Compositions and process for improving carbonatation clarification of sugar liquors and syrups |
| US9175358B2 (en) | 2009-11-11 | 2015-11-03 | Carbo-UA Limited | Compositions and processes for sugar treatment |
| US9605324B2 (en) | 2009-12-23 | 2017-03-28 | Carbo-UA Limited | Compositions and processes for clarification of sugar juices and syrups in sugar mills |
| CN102906279A (en) * | 2009-12-23 | 2013-01-30 | 卡博Ua有限公司 | Compositions and processes for clarification of sugar juices and syrups |
| CN103007624A (en) * | 2012-12-16 | 2013-04-03 | 西王药业有限公司 | Decolorizing active carbon recycle device and production technique |
| CN105238883A (en) * | 2015-10-27 | 2016-01-13 | 广西大学 | Purification and decoloring method of cane molasses |
| CN106319098A (en) * | 2016-09-26 | 2017-01-11 | 广西科技大学 | Sugar juice decoloring agent and sugar juice purification decoloring method |
| CN106319098B (en) * | 2016-09-26 | 2019-10-18 | 广西科技大学 | A kind of decolorizing agent for sugar juice and method for cleaning and decolorizing sugar juice |
| CN110305989A (en) * | 2019-07-08 | 2019-10-08 | 广西壮族自治区亚热带作物研究所(广西亚热带农产品加工研究所) | A kind of preparation method of mango brown sugar |
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