CN101798148A - Method for producing drinking water by utilizing steam condensation water of sugar refinery - Google Patents
Method for producing drinking water by utilizing steam condensation water of sugar refinery Download PDFInfo
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- CN101798148A CN101798148A CN 201010133314 CN201010133314A CN101798148A CN 101798148 A CN101798148 A CN 101798148A CN 201010133314 CN201010133314 CN 201010133314 CN 201010133314 A CN201010133314 A CN 201010133314A CN 101798148 A CN101798148 A CN 101798148A
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- water
- vapour
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- coagulate
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Abstract
The invention discloses a method for producing drinking water by utilizing steam condensation water of a sugar refinery. In the method, the steam condensation water of the sugar refinery is subjected to one, two or more devices of a sand leach device, an active carbon device, an ion exchange resin device, a reverse osmosis device and a nanofiltration device in order to reach the standard of the drinking water. The invention can effectively recycle the steam condensation water, increase the comprehensive utilization approaches for the sugar refinery, improve the economic benefit and can reduce the exhaust of the waste water of the sugar refinery.
Description
Technical field
The present invention relates to a kind of method of producing tap water, specifically is a kind of method of utilizing sugar refinery's evaporation vapour to coagulate aquatic producing drinking water.
Technical background
Water is Source of life, is indispensable important substance in human lives and the activity in production, is irreplaceable important natural resources.Along with the raising of Economic development, population growth and people's material and cultural life, growing to the demand of water all over the world, some countries and regions begin to have taken place the water crisis in the sixties in 20th century, and the problem of water has caused the common concern of contemporary world various countries.
Moisture about 75% is arranged in the sugarcane, in sugar manufacturing process, extract with sugar by the water of high pressure with this part, form the sugar soln about 15 ° of Bx, after clarifying treatment, revaporization, crystallization, after removing large quantity of moisture, form sucrose crystal and separate out.Day to handle 5000 tons of sugar refinery of sugarcane:
Cane sugar factory five imitate vapo(u)rization systems with clear juice from about 15 ° of Bx left and right sides evaporation concentration to 65 ° Bx, produce a large amount of secondary steams, have 3400 tons of vapour to coagulate water approximately.Wherein I is imitated the vapour of imitating steam with II to coagulate the water sugar degree low, and generally can be used as boiler and go into Lu Shui, but the 378 tons of residues of also having an appointment.At present this part water coagulates water as process water with the vapour that several effects in back produce, and discharges after reaching emission standard through handling, and causes very big waste and increases the pressure of terminal water treatment.
Remaining I, II are imitated vapour coagulate water treatment, make its standard that reaches tap water, barreled is sold, and both can reduce discharge of wastewater, can improve again and increase economic efficiency.
Summary of the invention
The object of the present invention is to provide a kind of devices purification sugar refinery evaporation vapour such as sand filtration, activated carbon, ion exchange resin, reverse osmosis, nanofiltration that utilize to coagulate water, make it reach a kind of method of producing tap water of straight drink guidelines for drinking water quality.
The technical scheme that the present invention solves the problems of the technologies described above is:
A kind of method of utilizing sugar refinery's evaporation vapour to coagulate aquatic producing drinking water, this method is vapour to be evaporated in sugar refinery coagulate water, coagulate water by one in sand filtration, activated carbon, ion exchange resin, reverse osmosis, the nanofiltration device, two or more combined treatment vapour, make it reach the index of tap water.
Above-mentioned sugar refinery evaporation vapour coagulate water be vapour that evaporation section vaporizer I or II are imitated coagulate water or I, II imitate vapour coagulate water by a certain percentage blended vapour coagulate water.
Above-mentioned sugar refinery evaporation vapour coagulate water by sand filtration, activated carbon, ion exchange resin, reverse osmosis, nanofiltration device one of them, two or more combined treatment, reach the index of tap water.
The present invention compared with prior art has following effect:
Technology of the present invention is simple, and the equipment maturation is when purifying treatment vapour coagulates water, selective retention some effective ingredients in plant, not only effectively recycling vapour coagulates water, increases sugar refinery comprehensive Utilization Ways, increase economic efficiency, also can reduce the wastewater from sugar plant discharging.
Embodiment
From the sugarcane plant, extract, the vapour that gets with evaporation coagulates water, rich in mineral substances and polyphenols antioxidant comprise brass, catechin, anthocyanidin etc., and method of the present invention is in purifying treatment, selective retention some effective ingredients in plant, have the good health care medical functions, can remove the intravital free radical of people, reduce its undesirable action HUMAN HEALTH, and can stimulating immune system produce antibody, reach effects such as antisepsis and anti-inflammation, antiviral, antianaphylaxis.Simultaneously, can replenish mineral substance and the trace element that human body needs.Not only effectively recycling vapour coagulates water, increases sugar refinery comprehensive Utilization Ways, increases economic efficiency, and also can reduce the wastewater from sugar plant discharging.
Below in conjunction with embodiment the present invention is further described.
Embodiment 1
Evaporation I is imitated vapour coagulate water, reach the index of tap water separately by one, two or more combined treatment of sand filtration, activated carbon, ion exchange resin, reverse osmosis, nanofiltration device.
Embodiment 2
Evaporation II is imitated vapour coagulate water, reach the index of tap water separately by one, two or more combined treatment of sand filtration, activated carbon, ion exchange resin, reverse osmosis, nanofiltration device.
Embodiment 3
To evaporate I, II and imitate vapour and coagulate water and mix by a certain percentage,, reach the index of tap water by, two or more combined treatment of sand filtration, activated carbon, ion exchange resin, reverse osmosis, nanofiltration device.
Claims (3)
1. one kind is utilized sugar refinery to evaporate the method that vapour coagulates aquatic producing drinking water, it is characterized in that: this method is vapour to be evaporated in sugar refinery coagulate water, by sand filtration, activated carbon, ion exchange resin, reverse osmosis, nanofiltration device one, two or more combined treatment vapour coagulate water, make it reach the index of tap water.
2. a kind of method of utilizing sugar refinery's evaporation vapour to coagulate aquatic producing drinking water according to claim 1, it is characterized in that, described sugar refinery evaporation vapour coagulate water be vapour that evaporation section vaporizer I or II are imitated coagulate water or I, II imitate vapour coagulate water by a certain percentage blended vapour coagulate water.
3. a kind of method of utilizing sugar refinery's evaporation vapour to coagulate aquatic producing drinking water according to claim 1, it is characterized in that, described sugar refinery evaporation vapour coagulate water by sand filtration, activated carbon, ion exchange resin, reverse osmosis, nanofiltration device one of them, two or more combined treatment, reach the index of tap water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010133314 CN101798148A (en) | 2010-03-26 | 2010-03-26 | Method for producing drinking water by utilizing steam condensation water of sugar refinery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201010133314 CN101798148A (en) | 2010-03-26 | 2010-03-26 | Method for producing drinking water by utilizing steam condensation water of sugar refinery |
Publications (1)
| Publication Number | Publication Date |
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| CN101798148A true CN101798148A (en) | 2010-08-11 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN 201010133314 Pending CN101798148A (en) | 2010-03-26 | 2010-03-26 | Method for producing drinking water by utilizing steam condensation water of sugar refinery |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102452702A (en) * | 2010-10-15 | 2012-05-16 | 中粮生物化学（安徽）股份有限公司 | Recycling method of condensed water |
| CN104193070A (en) * | 2014-09-26 | 2014-12-10 | 李仕全 | Effluent treatment device for sugarcane factory |
| CN104839827A (en) * | 2015-04-27 | 2015-08-19 | 广西大学 | Multistage-membrane apparatus for parallel production of concentrated sugarcane juice and sugarcane drinking water |
| CN106365251A (en) * | 2016-08-25 | 2017-02-01 | 山东省鲁洲食品集团有限公司 | Recovery method for starch syrup ion exchange material pressing water |
| CN106868228A (en) * | 2017-03-23 | 2017-06-20 | 广西大学 | A kind of processing equipment of embrane method sugaring concentrate |
| CN114590914A (en) * | 2022-02-11 | 2022-06-07 | 江苏久吾高科技股份有限公司 | Process for co-producing white granulated sugar from sugarcane plant drinking water |
| CN114891931A (en) * | 2022-03-01 | 2022-08-12 | 江苏久吾高科技股份有限公司 | Process for co-producing high-quality ginger-flavored brown sugar from sugarcane plant cell drinking water |
| CN114891930A (en) * | 2022-02-21 | 2022-08-12 | 江苏久吾高科技股份有限公司 | Method for co-production of high-quality original ecological brown sugar from sugarcane plant cell drinking water |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007107992A2 (en) * | 2006-03-20 | 2007-09-27 | B.P.T. - Bio Pure Technology Ltd. | Hybrid membrane module, system and process for treatment of industrial wastewater |
| CN101182088A (en) * | 2007-11-19 | 2008-05-21 | 广西工院糖业科技有限责任公司 | Novel technique for quality-preservation treatment of sugar plant circulation cooling water |
| CN101266102A (en) * | 2008-05-08 | 2008-09-17 | 陈志强 | Cane sugar factory waste water zero discharge process |
| CN101279780A (en) * | 2008-05-20 | 2008-10-08 | 钮德明 | Method for removing sugar of and purifying boiler water for sugar refinery |
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2010
- 2010-03-26 CN CN 201010133314 patent/CN101798148A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007107992A2 (en) * | 2006-03-20 | 2007-09-27 | B.P.T. - Bio Pure Technology Ltd. | Hybrid membrane module, system and process for treatment of industrial wastewater |
| CN101182088A (en) * | 2007-11-19 | 2008-05-21 | 广西工院糖业科技有限责任公司 | Novel technique for quality-preservation treatment of sugar plant circulation cooling water |
| CN101266102A (en) * | 2008-05-08 | 2008-09-17 | 陈志强 | Cane sugar factory waste water zero discharge process |
| CN101279780A (en) * | 2008-05-20 | 2008-10-08 | 钮德明 | Method for removing sugar of and purifying boiler water for sugar refinery |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102452702A (en) * | 2010-10-15 | 2012-05-16 | 中粮生物化学（安徽）股份有限公司 | Recycling method of condensed water |
| CN102452702B (en) * | 2010-10-15 | 2013-04-10 | 安徽中粮生化燃料酒精有限公司 | Recycling method of condensed water |
| CN104193070A (en) * | 2014-09-26 | 2014-12-10 | 李仕全 | Effluent treatment device for sugarcane factory |
| CN104193070B (en) * | 2014-09-26 | 2015-10-28 | 李仕全 | A kind of liquid waste treating apparatus of cane sugar factory |
| CN104839827A (en) * | 2015-04-27 | 2015-08-19 | 广西大学 | Multistage-membrane apparatus for parallel production of concentrated sugarcane juice and sugarcane drinking water |
| CN106365251A (en) * | 2016-08-25 | 2017-02-01 | 山东省鲁洲食品集团有限公司 | Recovery method for starch syrup ion exchange material pressing water |
| CN106868228A (en) * | 2017-03-23 | 2017-06-20 | 广西大学 | A kind of processing equipment of embrane method sugaring concentrate |
| CN114590914A (en) * | 2022-02-11 | 2022-06-07 | 江苏久吾高科技股份有限公司 | Process for co-producing white granulated sugar from sugarcane plant drinking water |
| CN114891930A (en) * | 2022-02-21 | 2022-08-12 | 江苏久吾高科技股份有限公司 | Method for co-production of high-quality original ecological brown sugar from sugarcane plant cell drinking water |
| CN114891931A (en) * | 2022-03-01 | 2022-08-12 | 江苏久吾高科技股份有限公司 | Process for co-producing high-quality ginger-flavored brown sugar from sugarcane plant cell drinking water |
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Open date: 20100811 |