CN201148389Y - Urea industrial production wastewater treatment plant - Google Patents
Urea industrial production wastewater treatment plant Download PDFInfo
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- CN201148389Y CN201148389Y CNU2008200962181U CN200820096218U CN201148389Y CN 201148389 Y CN201148389 Y CN 201148389Y CN U2008200962181 U CNU2008200962181 U CN U2008200962181U CN 200820096218 U CN200820096218 U CN 200820096218U CN 201148389 Y CN201148389 Y CN 201148389Y
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Abstract
Description
技术领域: Technical field:
本实用新型涉及废水处理设备,特别是一种尿素工业生产废水处理装置。The utility model relates to waste water treatment equipment, in particular to a waste water treatment device for urea industrial production.
背景技术: Background technique:
现有流行的处理技术是设置分列式设备来处理尿素废水,其主要工艺是A2/0法。这种工艺的缺点是:The existing popular treatment technology is to set up split-type equipment to treat urea wastewater, and its main process is the A 2 /0 method. The disadvantages of this process are:
1)工艺复杂,控制点多;1) The process is complex and there are many control points;
2)不耐尿素工业生产废水中有机物浓度低,NH3-N浓度高冲击负荷;2) Not resistant to low concentration of organic matter and high concentration of NH 3 -N in urea industrial production wastewater;
3)占地面积大,一次性投资高。3) It occupies a large area and requires a high one-time investment.
发明内容: Invention content:
本实用新型的目的在于提供一种尿素工业生产废水处理装置,利用该装置能达到将低浓度有机物和高浓度尿素废水处理达标排放的目的。The purpose of the utility model is to provide a urea industrial production wastewater treatment device, which can achieve the purpose of treating low-concentration organic matter and high-concentration urea wastewater to meet the standard discharge.
本实用新型的构成:由机械格栅、调节池、碳源罐、提升泵、SBR反应器、污泥浓缩池、污泥提升泵、污泥反应器、污泥干化设备、助凝剂投药箱、监护池、监护泵、事故池、事故泵、各种在线监测仪表和潜水搅拌机组成,生产废水进水管1与格栅槽2相连,在格栅槽2内装有机械格栅3,格栅槽2与调节池4连通,提升泵10通过提升泵进、出水管11分别与调节池4和SBR反应器12顶部相连,净水设备SBR反应器12安装在基础49上,SBR反应器12下部装有布风装置16,通过供风管15与高压风机14相连,SBR反应器12内装有滗水器13,通过排水管18入监护池35中,SBR反应器12内的排泥系统17通过手控阀门19、电控阀门20,由排泥管21接入污泥浓缩池22中;碳源罐7上装有虹吸式计量装置6,虹吸式计量装置6通过碳源投加管5接入格栅槽2内;The composition of the utility model: consists of a mechanical grid, a regulating tank, a carbon source tank, a lift pump, an SBR reactor, a sludge concentration tank, a sludge lift pump, a sludge reactor, sludge drying equipment, and coagulant aid dosing Tank, monitoring pool, monitoring pump, accident pool, accident pump, various online monitoring instruments and submersible mixer, the production wastewater inlet pipe 1 is connected to the grid tank 2, and the mechanical grid 3 is installed in the grid tank 2, the grid The tank 2 communicates with the regulating tank 4, and the lifting pump 10 is connected to the top of the regulating tank 4 and the SBR reactor 12 through the lifting pump inlet and
事故废水进水管39与格栅槽40相连,格栅槽40内装有机械格栅41,格栅槽40与事故池42相连,事故泵43通过事故泵进、出水管44与事故池42和调节池4相连;在监护池35上装有达标水排放管34,监护泵36通过不合格水回流管37分别与监护池35、调节池4和超越管46相连,超越管46连接事故池42;The accident
污泥浓缩池22上装有排泥管21和上清液回流管33,上清液回流管33与滤液回流管32相连,污泥提升泵24通过污泥泵吸泥管23与污泥浓缩池22连接,通过污泥泵出泥管25与污泥反应器26连接,污泥反应器26通过反应器出泥管27与污泥干化设备28连接,污泥干化设备28通过滤液回流管32与调节池4连接,助凝剂投加箱31上装有助凝剂计量泵30,助凝剂计量泵30通过助凝剂投加管29与污泥泵出泥管25连接。The sludge concentration tank 22 is equipped with a sludge discharge pipe 21 and a supernatant liquid return pipe 33, the supernatant liquid return pipe 33 is connected with the
在调节池4、SBR反应器12、监护池35和事故池42内安装潜水搅拌机47。A
在调节池4内装有在线监测仪表48,在监护池35中安装NH3-N和COD在线监测仪38,在SBR反应器12内还安装有DO、ORP、MLSS在线监测仪表。An on-line monitoring instrument 48 is installed in the regulating pool 4, an online monitoring instrument 38 for NH 3 -N and COD is installed in the
在提升泵进、出水管11上装有用法兰连接的出水电控阀9、手动控制阀8和超越阀45,超越管46与超越阀45相连,并接入事故池42。On the inlet and
与现有技术比较,本实用新型将合成氨、尿素、硝酸铵、碳酸氢胺等工业生产废水处理到达标排放水平,特别是一种以SBR反应器为核心的净水装置,能将低浓度有机物和高浓度尿素废水处理达标排放,而且实现了占地面积少、投资少、见效快、出水水质稳定、管理方便和自动化运行。Compared with the prior art, the utility model treats industrial production wastewater such as synthetic ammonia, urea, ammonium nitrate, and ammonium bicarbonate to meet the standard discharge level, especially a water purification device with the SBR reactor as the core, which can remove low-concentration organic matter And high-concentration urea wastewater treatment meets the discharge standards, and realizes small footprint, low investment, quick results, stable effluent quality, convenient management and automatic operation.
附图说明: Description of drawings:
附图是本实用新型结构示意图。Accompanying drawing is the structural representation of the utility model.
图中1.生产废水进水管,2.格栅槽,3.机械格栅,4.调节池,5.碳源投加管,6.虹吸式计量装置,7.碳源罐,8.手动控制阀,9.出水电控阀,10.提升泵,11.提升泵进、出水管,12.SBR反应器,13.滗水器,14.高压风机,15.供风管,16.布风装置,17.排泥系统,18.排水管,19.手控阀门,20.电控阀门,21.排泥管,22.污泥浓缩池,23.污泥泵吸泥管,24.污泥提升泵,25.污泥泵出泥管,26.污泥反应器,27.反应器出泥管,28.污泥干化设备,29.助凝剂投加管,30.助凝剂计量泵,31.助凝剂投加箱,32.滤液回流管,33.上清液回流管,34.达标水排放管,35.监护池,36.监护泵,37.不合格水回流管,38.NH3-N和COD在线监测仪,39.事故废水进水管,40.格栅槽,41.机械格栅,42.事故池,43.事故泵,44.事故泵进、出水管,45.超越阀,46.超越管,47.潜水搅拌机,48.在线监测仪表,49.基础。In the figure 1. Production wastewater inlet pipe, 2. Grille tank, 3. Mechanical grille, 4. Adjusting tank, 5. Carbon source dosing pipe, 6. Siphon metering device, 7. Carbon source tank, 8. Manual Control valve, 9. Water outlet electric control valve, 10. Lift pump, 11. Lift pump inlet and outlet pipes, 12. SBR reactor, 13. Decanter, 14. High pressure fan, 15. Air supply pipe, 16. Cloth Wind device, 17. Sludge discharge system, 18. Drainage pipe, 19. Manual valve, 20. Electric control valve, 21. Sludge discharge pipe, 22. Sludge concentration tank, 23. Sludge pump suction pipe, 24. Sludge lifting pump, 25. Sludge pump outlet pipe, 26. Sludge reactor, 27. Reactor sludge outlet pipe, 28. Sludge drying equipment, 29. Coagulant dosing pipe, 30. Coagulation aid Agent metering pump, 31. Coagulant dosing box, 32. Filtrate return pipe, 33. Supernatant liquid return pipe, 34. Standard water discharge pipe, 35. Monitoring pool, 36. Monitoring pump, 37. Unqualified water return Pipe, 38. NH 3 -N and COD online monitor, 39. Accident wastewater inlet pipe, 40. Grille tank, 41. Mechanical grille, 42. Accident pool, 43. Accident pump, 44. Accident pump inlet and outlet Water pipe, 45. Overrun valve, 46. Override tube, 47. Submersible mixer, 48. Online monitoring instrument, 49. Foundation.
具体实施方式: Detailed ways:
如图所示,1.进水与调节池:生产废水进水管1与格栅槽2相连,并进入其中,格栅槽2内装有机械格栅3,格栅槽2与调节池4相连并相通,调节池4内安装潜水搅拌机47、提升泵进、出水管11、滤液回流管32、不合格水回流管37和在线监测仪表48。2.提升系统:提升泵10上装有提升泵进、出水管11接入SBR反应器12中;提升泵进、出水管11上还装有用法兰连接的出水电控阀9、超越阀45和手动控制阀8;超越管46与超越阀45相连,并接入事故池42中。3.净水设备:1)净水设备SBR反应器12为钢结构或钢筋砼结构,安装在基础49上。2)进水系统:SBR反应器12顶部装有进水管11。3)供风系统;SBR反应器12下部装有布风装置16,与供风管15相连,供风管15与高压风机14相连。4)排水系统;SBR反应器12内装有滗水器13接出器外,与排水管18相连,排水管18接入监护池35中。滗水器的形成可以根据自控水平设置。5)搅拌装置;SBR反应器12内装有潜水搅拌机47。6)排泥系统:SBR反应器12内装有排泥系统17接出器外,与手控阀门19、电控阀门20用法兰盘相连接,电控阀门20与排泥管21相连,排泥管21接入污泥浓缩池22中。7)在线监测仪表:SBR反应器12内还安装有DO、ORP、MLSS等在线监测仪表,可以根据自控水平设置。As shown in the figure, 1. Water inlet and regulating tank: the production waste water inlet pipe 1 is connected to the grid tank 2 and enters it. The mechanical grid 3 is installed in the grid tank 2, and the grid tank 2 is connected to the regulating tank 4 and Connected,
4.营养源补充:碳源罐7上装有虹吸式计量装置6,也可用计量泵类;虹吸式计量装置6与碳源投加管5相连,碳源投加管5接入格栅槽2内。4. Nutrient source supplementation: the carbon source tank 7 is equipped with a siphon metering device 6, and a metering pump can also be used; the siphon metering device 6 is connected with the carbon
5.事故系统:事故废水进水管39与格栅槽40相连,并进入槽中;格栅槽40内装有机械格栅41;格栅槽40与事故池42相连,并相通;事故池42内装有潜水搅拌机47和事故泵进、出水管44;事故泵43与事故泵进、出水管44相连;事故泵进、出水管44接入调节池4中。5. Accident system: the accident waste
6.监护系统:监护池35内装有潜水搅拌机47、NH3-N和COD在线监测仪38,达标水排放管34自监护池35接出,监护池35内装有不合格水回流管37与监护泵36相连,不合格水回流管37接进调节池4中,并与超越管46相连。6. Monitoring system:
7.污泥处理系统:污泥浓缩池22上装有排泥管21、上清液回流管33,上清液回流管33与滤液回流管32相连接,污泥浓缩池22内还装有污泥泵吸泥管23,污泥泵吸泥管23与污泥提升泵24吸口相连接,污泥提升泵24出口装有污泥泵出泥管25并接进污泥反应器26中,污泥反应器26下端接反应器出泥管27,反应器出泥管27接进污泥干化设备28中,污泥干化设备的形式可根据需要选择,自污泥干化设备28中接出滤液回流管32,并接入调节池4中;助凝剂投加箱31上装有助凝剂计量泵30,助凝剂计量泵30出口装有助凝剂投加管29,助凝剂投加管29与污泥泵出泥管25相接通。7. Sludge treatment system: the sludge concentration tank 22 is equipped with a sludge discharge pipe 21 and a supernatant liquid return pipe 33, the supernatant liquid return pipe 33 is connected with the
工作原理:working principle:
尿素工业生产废水从进水管1进入格栅槽2,流过机械格栅3,截流大块悬浮物,以免堵塞后续设备,过栅水流入调节池4调节水量、均化水质,保证后续设备负荷均匀,提升泵10按SBR进水周期要求运行,将调节池水送入SBR反应器12,SBR反应器经过进水、曝气、沉淀、滗水和闲置等工序依次完成一个处理周期,由SBR反应器12内的滗水器排出的处理水进入监护池35,在监护池内所配COD等在线监测仪38,在其监测下,合格水排放,而完成整个水处理工艺流程。The urea industrial production wastewater enters the grid tank 2 from the water inlet pipe 1, flows through the mechanical grid 3, intercepts large suspended solids, and avoids blocking subsequent equipment, and the water passing through the grid flows into the regulating tank 4 to adjust the water volume and homogenize the water quality to ensure the load of subsequent equipment Evenly, the lift pump 10 operates according to the requirements of the SBR water intake cycle, and sends the regulating pool water into the SBR reactor 12. The SBR reactor completes a treatment cycle in sequence through the processes of water intake, aeration, sedimentation, decanting, and idleness, and is reacted by the SBR. The treated water discharged from the decanter in the device 12 enters the
营养源补充与搅拌;由于生化处理工艺要求C/N≥3时才有较好的生化条件,而合成氨生产废水中C和N之比经常达不到要求,故必须适时向调节池投加生化性强的碳源,碳源由碳源罐7经过虹吸式计量装置6投加到调节池4中。在调节池4中设有潜水搅拌机47适时搅拌,并保证污泥不沉底和起到相当的生化予反应作用。Supplementation and stirring of nutrient sources; since the biochemical treatment process requires C/N ≥ 3 to have better biochemical conditions, and the ratio of C and N in the synthetic ammonia production wastewater often fails to meet the requirements, it is necessary to add biochemicals to the adjustment tank in due course Strong carbon source, the carbon source is added into the regulating pool 4 by the carbon source tank 7 through the siphon metering device 6 . In the adjustment tank 4, a
供风系统:当SBR反应器12需要供风时,风源由高压风机14送入SBR反应器12内布风装置16进行曝气。Air supply system: When the SBR reactor 12 needs air supply, the air source is sent from the high-pressure fan 14 to the air distribution device 16 in the SBR reactor 12 for aeration.
出水系统:当SBR反应器12到达排水工序时,由滗水器13执行滗水,将上清液送入监护池35,经在线监测仪38监测合格时从达标水排放管34排放。Water outlet system: When the SBR reactor 12 reaches the drainage process, the decanter 13 performs decanting, and the supernatant is sent to the
排泥:当SBR反应器12需要排泥时,开启电控阀门20,SBR反应器12中的污泥经排泥系统17收集排入污泥浓缩池22中浓缩。Sludge discharge: When the SBR reactor 12 needs to discharge sludge, open the electronic control valve 20, and the sludge in the SBR reactor 12 is collected by the sludge discharge system 17 and discharged into the sludge thickening tank 22 for concentration.
事故保障系统;事故废水一般有以下三类:1)初雨水、消防事故水和设备事故或维修废水,这些废水成分复杂、浓度高,由事故废水进水管39流入格栅槽40,经机械格栅41拦去大块悬浮物后流入事故池42,再经事故泵43按净水设备可接受的流星送入调节池4参与处理。为了均化水质防止沉淀,事故池42内装有潜水搅拌机47。2)尿素不成比例废水:当调节池中NH3-N与COD不成生化比例时,用提升泵10提升,经超越阀45和超越管46送入事故池42。3)SBR反应器不合格水:当监护池35中出现不达标水时,用监护泵36送回调节池4或事故池42参与再处理。Accident protection system; accident wastewater generally has the following three categories: 1) early rainwater, fire accident water and equipment accident or maintenance wastewater, these wastewater components are complex and high in concentration, and flow into the grid groove 40 by the accident
污泥处理系统:污泥在污泥浓缩池22中浓缩后,上清液流回调节池4,污泥用污泥提升泵24提升,送入压力式污泥反应器26内与从助凝剂投加箱31、助凝剂计量泵30送来的助凝剂反应,反应污泥压入污泥干化设备28,干泥运出,出水送回调节池4。Sludge treatment system: After the sludge is concentrated in the sludge thickening tank 22, the supernatant flows back to the regulating tank 4, and the sludge is lifted by the sludge lifting pump 24, and then sent into the
自动控制:SBR反应器自控:SBR反应器为间隙式生化处理工艺,它的反应可分为进水、曝气、沉淀、滗水与闲置五个阶段来完成,它的运行主要靠各种仪表监测与PLC自动控制来完成。Automatic control: SBR reactor automatic control: SBR reactor is an intermittent biochemical treatment process. Its reaction can be divided into five stages: water intake, aeration, sedimentation, decanting and idleness. Its operation mainly depends on various instruments Monitoring is done with PLC automatic control.
进水阶段;当SBR反应器12过了闲置阶段后,进入下一个处理周期,则指令提升泵10按进水历时向SBR反应器12进水,到时间自动停泵。Water intake stage; when the SBR reactor 12 passes the idle stage and enters the next processing cycle, the lift pump 10 is instructed to feed water into the SBR reactor 12 according to the water intake duration, and the pump is automatically stopped when the time is up.
曝气阶段:在进水后指令变频高压风机14按曝气历时供风,到时间停机,其供风量按控制仪表DO在线监测仪测试水中溶解氧指导风机变频,调整供风量,另有ORP在线监测仪判断好氧阶段的氧化还原能力,即SBR的处理能力,以此调整曝气周期。Aeration stage: After water intake, command the variable frequency high-pressure fan 14 to supply air according to the aeration duration, and stop at the time, and the air supply volume will be controlled according to the DO online monitor to test the dissolved oxygen in the water, guide the fan frequency conversion, adjust the air supply volume, and ORP online The monitor judges the redox capacity of the aerobic stage, that is, the processing capacity of the SBR, and adjusts the aeration cycle accordingly.
沉淀阶段:这阶段不开任何设备,按沉淀历时进行。Precipitation stage: No equipment is turned on at this stage, and it is carried out according to the duration of precipitation.
排水阶段:沉淀结束后,指令滗水器13按排水历时实行滗水,滗水器可采用目前常用的产品,但必须可以自动调节排水流量和排水历时的。Drainage stage: after the sedimentation is over, instruct the decanter 13 to decant water according to the duration of drainage. The decanter can use the products commonly used at present, but it must be able to automatically adjust the drainage flow and the duration of drainage.
闲置阶段:按闲置历时,自动开启安装在SBR反应器12中的潜水搅拌机47,进行缺氧、厌氧反应,在闲置阶段完全毕后,设备进入下轮处理工序循环。Idle stage: according to the idle period, the
排泥:SBR反应器12中装有MLSS在线监测仪,监测反应器内污泥浓度,当MLSS>8000mg/L时,指令自动开启排泥阀20排泥。排泥量按规定MLSS指标监测确定。Sludge discharge: The SBR reactor 12 is equipped with an MLSS online monitor to monitor the sludge concentration in the reactor. When the MLSS>8000mg/L, the command automatically opens the sludge discharge valve 20 to discharge the sludge. The amount of mud discharge shall be monitored and determined according to the specified MLSS indicators.
监护池自控:SBR反应器12的出水排入监护池35,当池内NH3-N和COD在线监测仪监测池水不合格时,指令监护泵36自动开启,将不合格水返回调节池4或事故池42参与再处理,直到监护泵36中来水合格为止。Self-control of the monitoring pool: the effluent of the SBR reactor 12 is discharged into the
调节池水质控制:调节池4内装有PH、COD、NH3-N和液位传感器等在线监测仪表48,来监测池中各项水质,当池水监测指标不符合SBR12处理指标时,则指令关闭水泵出水电控阀9,开启提升泵10和超越阀45,将该水送入事故池42待处理。Water quality control in the regulating pool: the regulating pool 4 is equipped with online monitoring instruments 48 such as PH, COD, NH 3 -N and liquid level sensors to monitor the water quality in the pool. When the monitoring index of the pool water does not meet the SBR12 treatment index, the command is closed The water pump discharges the electric control valve 9, opens the lift pump 10 and the overrun valve 45, and sends the water into the
其它系统:其它系统如碳源投加、机械格栅、潜水搅拌机、事故泵、消毒及污泥处理系统均可采用一般的自控程序。Other systems: Other systems such as carbon source dosing, mechanical grille, submersible mixer, emergency pump, disinfection and sludge treatment systems can adopt general self-control procedures.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102557359A (en) * | 2012-03-01 | 2012-07-11 | 贵州绿色环保设备工程有限责任公司 | Device for treating wastewater during production of pentaerythritol |
| CN106348524A (en) * | 2016-08-30 | 2017-01-25 | 芜湖华海生物工程有限公司 | Treatment process for high-concentration allantoin production wastewater |
| CN108862927A (en) * | 2018-07-26 | 2018-11-23 | 江苏开放大学(江苏城市职业学院) | A kind of printing and dyeing wastewater processing equipment and its application |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102557359A (en) * | 2012-03-01 | 2012-07-11 | 贵州绿色环保设备工程有限责任公司 | Device for treating wastewater during production of pentaerythritol |
| CN106348524A (en) * | 2016-08-30 | 2017-01-25 | 芜湖华海生物工程有限公司 | Treatment process for high-concentration allantoin production wastewater |
| CN108862927A (en) * | 2018-07-26 | 2018-11-23 | 江苏开放大学(江苏城市职业学院) | A kind of printing and dyeing wastewater processing equipment and its application |
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