CN102531283A - Method for treating food processing organic wastewater containing high-concentration fat and suspended matter - Google Patents
Method for treating food processing organic wastewater containing high-concentration fat and suspended matter Download PDFInfo
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- CN102531283A CN102531283A CN2011104508175A CN201110450817A CN102531283A CN 102531283 A CN102531283 A CN 102531283A CN 2011104508175 A CN2011104508175 A CN 2011104508175A CN 201110450817 A CN201110450817 A CN 201110450817A CN 102531283 A CN102531283 A CN 102531283A
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- 239000002351 wastewater Substances 0.000 title claims abstract description 18
- 238000000034 method Methods 0.000 title claims abstract description 17
- 230000003068 static effect Effects 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000004519 grease Substances 0.000 claims abstract description 8
- 229910052751 metal Inorganic materials 0.000 claims abstract description 4
- 239000002184 metal Substances 0.000 claims abstract description 4
- 239000010815 organic waste Substances 0.000 claims abstract description 4
- 239000013049 sediment Substances 0.000 claims abstract description 4
- 239000007787 solid Substances 0.000 claims description 15
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 claims description 14
- 230000001105 regulatory effect Effects 0.000 claims description 9
- 230000003647 oxidation Effects 0.000 claims description 6
- 238000007254 oxidation reaction Methods 0.000 claims description 6
- 238000004062 sedimentation Methods 0.000 claims description 6
- 239000005416 organic matter Substances 0.000 claims description 5
- 238000005189 flocculation Methods 0.000 claims description 3
- 230000016615 flocculation Effects 0.000 claims description 3
- 238000009280 upflow anaerobic sludge blanket technology Methods 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 2
- 239000007788 liquid Substances 0.000 description 2
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
一种处理含高油脂、高悬浮物的食品加工有机废水方法,其特征是方法为:含高油脂、高悬浮物的食品加工有机废水经车间排水沟流入静置池,排水沟中设有若干个金属格栅滤网,网格从4~10目不等,以截留较大的悬浮物;静置池中设了上下隔油板,废水在静置池中静置1-2d,悬浮在表面的油脂被上隔油板挡住,沉积在底部的沉渣用下隔油板挡住,达到了国家排放标准(GB8978-1996)中的二级排放标准。本发明的技术效果是:可持续处理废水,并且采用物理处理方法,成本低,易得到普及使用,最大限度减少污染。A method for treating food processing organic wastewater containing high fat and high suspended matter, characterized in that the method is: the organic waste water from food processing containing high fat and high suspended matter flows into the standing pool through the workshop drainage ditch, and several A metal grille filter screen, the mesh ranges from 4 to 10 meshes, to intercept larger suspended matter; the upper and lower oil separators are set in the static pool, and the wastewater is allowed to stand in the static pool for 1-2 days, suspended in the The grease on the surface is blocked by the upper oil separator, and the sediment deposited on the bottom is blocked by the lower oil separator, which meets the second-level emission standard in the national emission standard (GB8978-1996). The technical effect of the invention is that waste water can be treated sustainably, and the physical treatment method is adopted, the cost is low, the method is easy to be popularized and used, and the pollution is minimized.
Description
技术领域 technical field
本发明涉及一种有机废水处理方法,尤其涉及一种处理含高油脂、高悬浮物的食品加工有机废水方法。 The invention relates to a method for treating organic wastewater, in particular to a method for treating food processing organic wastewater containing high fat and high suspended matter.
背景技术 Background technique
在食品加工过程中会出现大量含高油脂、高悬浮物的食品有机废水,如果废水不经过处理直接排入江河会严重破坏生态环境,为了处理这些有机废水,现有方法处理成本高,难以普及使用。 In the process of food processing, there will be a large amount of food organic wastewater containing high fat and high suspended solids. If the wastewater is directly discharged into the river without treatment, it will seriously damage the ecological environment. In order to treat these organic wastewater, the existing methods are expensive and difficult to popularize. use.
发明内容 Contents of the invention
本发明的目的在于提供一种处理含高油脂、高悬浮物的食品加工有机废水方法,采用物理处理的方式,减少二次污染,使用成本低。 The purpose of the present invention is to provide a method for treating food processing organic wastewater containing high fat and high suspended solids, which adopts physical treatment, reduces secondary pollution, and has low use cost.
本发明是这样实现的,方法为:含高油脂、高悬浮物的食品加工有机废水经车间排水沟流入静置池,排水沟中设有若干个金属格栅滤网,网格从4~10目不等,以截留较大的悬浮物;静置池中设了上下隔油板, 废水在静置池中静置1-2d,油脂悬浮物基本上悬浮在表面,表面可达1~2 cm厚的粘性油脂,也有少量的较重的固形物沉积底部,中上部位的悬浮物较少,悬浮在表面的油脂被上隔油板挡住,沉积在底部的沉渣用下隔油板挡住,定期用泵排出, 静置池中出水口设在中上部;静置池的水自流入调节池,调节池起到调节水量水质的作用;调节池的废水用泵泵入BASB厌氧反应器进行厌氧处理,可以去除大部分的有机物; UASB反应器的出水自流入生物接触氧化池进一步去除剩余的有机物;生物接触氧化池的出水自流入絮凝沉淀池,在该池中的进口处用水力搅拌形式投加量为质量分数3‰~5‰碱式氯化铝(液体碱式氯化铝,固体碱式氯化铝4倍稀释),沉淀池中的出水最终达标排放,达到了国家排放标准(GB8978-1996)中的二级排放标准。 The present invention is realized in this way, the method is: the food processing organic waste water that contains high fat, high suspended solids flows into the standing pool through the workshop drainage ditch, and several metal grid filter screens are arranged in the drainage ditch, and the grids are from 4 to 10 The mesh is different to intercept larger suspended solids; the upper and lower oil separators are set in the static tank, and the wastewater is allowed to stand in the static tank for 1-2 days, and the grease suspended solids are basically suspended on the surface, and the surface can reach 1-2 cm thick viscous grease, there is also a small amount of heavy solids deposited at the bottom, and the suspended solids in the middle and upper parts are less, the grease suspended on the surface is blocked by the upper oil separator, and the sediment deposited at the bottom is blocked by the lower oil separator. Regularly use the pump to discharge, and the water outlet in the static pool is set at the middle and upper part; the water in the static pool flows into the regulating pool, and the regulating pool plays the role of regulating the water quantity and quality; the wastewater in the regulating pool is pumped into the BASB anaerobic reactor for treatment. Anaerobic treatment can remove most of the organic matter; the effluent of the UASB reactor flows into the biological contact oxidation tank to further remove the remaining organic matter; the effluent of the biological contact oxidation tank flows into the flocculation sedimentation tank, and is hydraulically stirred at the inlet of the tank Formal dosage is mass fraction 3‰~5‰ basic aluminum chloride (liquid basic aluminum chloride, solid basic aluminum chloride 4 times diluted), the effluent in the sedimentation tank finally reaches the standard discharge, reaching the national discharge standard (GB8978-1996) in the secondary emission standards.
本发明的技术效果是:可持续处理废水,并且采用物理处理方法,成本低,易得到普及使用,最大限度减少污染。 The technical effect of the invention is that waste water can be treated sustainably, and the physical treatment method is adopted, the cost is low, the method is easy to be popularized and used, and the pollution is minimized.
具体实施方式 Detailed ways
本发明是这样实现的,方法为:含高油脂、高悬浮物的食品加工有机废水经车间排水沟流入静置池,排水沟中设有若干个金属格栅滤网,网格从4~10目不等,以截留较大的悬浮物;静置池中设了上下隔油板, 废水在静置池中静置1-2d,油脂悬浮物基本上悬浮在表面,表面可达1~2 cm厚的粘性油脂,也有少量的较重的固形物沉积底部,中上部位的悬浮物较少,悬浮在表面的油脂被上隔油板挡住,沉积在底部的沉渣用下隔油板挡住,定期用泵排出, 静置池中出水口设在中上部;静置池的水自流入调节池,调节池起到调节水量水质的作用;调节池的废水用泵泵入BASB厌氧反应器进行厌氧处理,可以去除大部分的有机物; UASB反应器的出水自流入生物接触氧化池进一步去除剩余的有机物;生物接触氧化池的出水自流入絮凝沉淀池,在该池中的进口处用水力搅拌形式投加量为质量分数3‰~5‰碱式氯化铝(液体碱式氯化铝,固体碱式氯化铝4倍稀释),沉淀池中的出水最终达标排放,达到了国家排放标准(GB8978-1996)中的二级排放标准。 The present invention is realized in this way, the method is: the food processing organic waste water that contains high fat, high suspended solids flows into the standing pool through the workshop drainage ditch, and several metal grid filter screens are arranged in the drainage ditch, and the grids are from 4 to 10 The mesh is different to intercept larger suspended solids; the upper and lower oil separators are set in the static tank, and the wastewater is allowed to stand in the static tank for 1-2 days, and the grease suspended solids are basically suspended on the surface, and the surface can reach 1-2 cm thick viscous grease, there is also a small amount of heavy solids deposited at the bottom, and the suspended solids in the middle and upper parts are less, the grease suspended on the surface is blocked by the upper oil separator, and the sediment deposited at the bottom is blocked by the lower oil separator. Regularly use the pump to discharge, and the water outlet in the static pool is set at the middle and upper part; the water in the static pool flows into the regulating pool, and the regulating pool plays the role of regulating the water quantity and quality; the wastewater in the regulating pool is pumped into the BASB anaerobic reactor for treatment. Anaerobic treatment can remove most of the organic matter; the effluent of the UASB reactor flows into the biological contact oxidation tank to further remove the remaining organic matter; the effluent of the biological contact oxidation tank flows into the flocculation sedimentation tank, and is hydraulically stirred at the inlet of the tank Formal dosage is mass fraction 3‰~5‰ basic aluminum chloride (liquid basic aluminum chloride, solid basic aluminum chloride 4 times diluted), the effluent in the sedimentation tank finally reaches the standard discharge, reaching the national discharge standard (GB8978-1996) in the secondary emission standards.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103508641A (en) * | 2013-10-28 | 2014-01-15 | 波鹰(厦门)科技有限公司 | A kind of high-fat food processing wastewater treatment method |
CN103508642A (en) * | 2013-10-28 | 2014-01-15 | 波鹰(厦门)科技有限公司 | High-fat food processing wastewater treatment device |
CN103524002A (en) * | 2013-10-28 | 2014-01-22 | 波鹰(厦门)科技有限公司 | A high-fat food processing wastewater treatment device |
CN108975629A (en) * | 2018-08-20 | 2018-12-11 | 朱翠帮 | A kind of sewage treatment process of high oil mass |
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JP3693320B2 (en) * | 2000-09-06 | 2005-09-07 | 株式会社荏原製作所 | Method and apparatus for methane fermentation treatment of organic waste |
CN101224937A (en) * | 2008-02-01 | 2008-07-23 | 浙江嘉澳化工有限公司 | Reuse treating method for chemical industrial plasticizer waste water |
CN101462816A (en) * | 2009-01-12 | 2009-06-24 | 浙江大学 | Apparatus for integrated treatment and comprehensive utilization of wastewater and use thereof |
CN101475286A (en) * | 2009-01-14 | 2009-07-08 | 滁州润海甜叶菊高科有限公司 | Sewage treatment method for stevioside production line |
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2011
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Patent Citations (4)
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JP3693320B2 (en) * | 2000-09-06 | 2005-09-07 | 株式会社荏原製作所 | Method and apparatus for methane fermentation treatment of organic waste |
CN101224937A (en) * | 2008-02-01 | 2008-07-23 | 浙江嘉澳化工有限公司 | Reuse treating method for chemical industrial plasticizer waste water |
CN101462816A (en) * | 2009-01-12 | 2009-06-24 | 浙江大学 | Apparatus for integrated treatment and comprehensive utilization of wastewater and use thereof |
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Non-Patent Citations (1)
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103508641A (en) * | 2013-10-28 | 2014-01-15 | 波鹰(厦门)科技有限公司 | A kind of high-fat food processing wastewater treatment method |
CN103508642A (en) * | 2013-10-28 | 2014-01-15 | 波鹰(厦门)科技有限公司 | High-fat food processing wastewater treatment device |
CN103524002A (en) * | 2013-10-28 | 2014-01-22 | 波鹰(厦门)科技有限公司 | A high-fat food processing wastewater treatment device |
CN103508641B (en) * | 2013-10-28 | 2015-02-04 | 波鹰(厦门)科技有限公司 | Method for treating high-fat food processing wastewater |
CN103508642B (en) * | 2013-10-28 | 2015-05-06 | 波鹰(厦门)科技有限公司 | High-grease food processing wastewater treatment device |
CN103524002B (en) * | 2013-10-28 | 2015-08-26 | 波鹰(厦门)科技有限公司 | High grease food processing effluent treatment plant |
CN108975629A (en) * | 2018-08-20 | 2018-12-11 | 朱翠帮 | A kind of sewage treatment process of high oil mass |
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Application publication date: 20120704 |