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 PDF

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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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杨沂凤
邱俊明
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Nanchang University
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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

一种处理含高油脂、高悬浮物的食品加工有机废水方法A method for treating food processing organic wastewater containing high fat and high suspended solids

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.

Claims (1)

1. 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,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,调节池的废水用泵泵入BASB厌氧反应器进行厌氧处理, 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,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。 1. A method for processing 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 drain, and the drain is set There are a number of metal grille screens, ranging from 4 to 10 meshes, to intercept larger suspended solids; the upper and lower oil separators are set in the static pool, and the waste water is allowed to stand in the static pool for 1-2 days. 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, and is regularly discharged by a pump. 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 by itself. The wastewater in the adjustment tank is pumped into the BASB anaerobic reactor for anaerobic treatment. The effluent from the UASB reactor flows into the biological contact oxidation tank to further remove the remaining organic matter; the effluent from the biological contact oxidation tank flows into the flocculation sedimentation tank. The dosage of hydrodynamic stirring at the inlet is 3‰~5‰ basic aluminum chloride, and the effluent in the sedimentation tank finally reaches the standard discharge, reaching the second-level discharge standard in the national discharge standard (GB8978-1996). .
CN2011104508175A 2011-12-30 2011-12-30 Method for treating food processing organic wastewater containing high-concentration fat and suspended matter Pending CN102531283A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
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
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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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Title
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Cited By (7)

* Cited by examiner, † Cited by third party
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