CN106830562A - A kind of petrochemical industry wastewater treatment integrated technique system and method - Google Patents

A kind of petrochemical industry wastewater treatment integrated technique system and method Download PDF

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CN106830562A
CN106830562A CN201710177218.8A CN201710177218A CN106830562A CN 106830562 A CN106830562 A CN 106830562A CN 201710177218 A CN201710177218 A CN 201710177218A CN 106830562 A CN106830562 A CN 106830562A
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于鹏飞
李微
刘军
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Suzhou Hongsheng Environmental Protection Technology Co ltd
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Shenyang Jianzhu University
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    • C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
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    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/463—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrocoagulation
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    • C02F1/72—Treatment of water, waste water, or sewage by oxidation
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    • C02F2103/34—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
    • C02F2103/36—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the manufacture of organic compounds
    • C02F2103/365—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the manufacture of organic compounds from petrochemical industry (e.g. refineries)
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Abstract

本发明提供一种石油化工工业废水处理集成工艺系统及方法,所述系统包括在线监测分析系统、智能反馈控制系统、废水处理系统;所述在线监测分析系统用于对石油化工工业废水的水质成分及各个处理环节出水的水质成分进行监测分析,并将监测分析数据传送至所述智能反馈控制系统;所述智能反馈控制系统对所述监测分析数据处理后输出控制信号至所述废水处理系统;所述废水处理系统包括预处理模块、除油模块、生化模块、污泥处理模块及深度处理模块;所述预处理模块、除油模块、生化模块、深度处理模块及污泥处理模块根据智能反馈控制系统输出的控制信号指令对石油化工工业废水进行处理。所述方法经过7步获得SS、COD、色度等指标稳定达标的处理水。

The present invention provides an integrated process system and method for petrochemical industrial wastewater treatment. The system includes an online monitoring and analysis system, an intelligent feedback control system, and a wastewater treatment system; the online monitoring and analysis system is used to analyze the water quality components of petrochemical industrial wastewater Monitor and analyze the water quality components of the effluent from each treatment link, and transmit the monitoring and analysis data to the intelligent feedback control system; the intelligent feedback control system outputs control signals to the wastewater treatment system after processing the monitoring and analysis data; The wastewater treatment system includes a pretreatment module, an oil removal module, a biochemical module, a sludge treatment module and an advanced treatment module; the pretreatment module, an oil removal module, a biochemical module, an advanced treatment module and a sludge treatment module are The control signal output by the control system commands the petrochemical industrial wastewater to be treated. The method obtains the treated water whose indicators such as SS, COD, chroma and so on reach the standard stably through seven steps.

Description

一种石油化工工业废水处理集成工艺系统及方法An integrated process system and method for petrochemical industrial wastewater treatment

技术领域technical field

本发明属于工业废水处理技术领域,具体涉及一种石油化工工业废水处理集成工艺系统及方法。The invention belongs to the technical field of industrial wastewater treatment, and in particular relates to an integrated process system and method for petrochemical industrial wastewater treatment.

背景技术Background technique

石油化工是以石油、天然气等为原料,加工成各种化工产品的工业。石油化工废水是石油化工企业生产过程排出的废水,污水来源节点分布在各生产装置、原油罐区、供排水车间等处。石油化工废水中物质种类繁多,组成复杂,有机物含量高,COD约为600~1200mg/L,BOD为200~1000mg/L;由于生产过程中使用催化剂种类较多,废水中含有多种重金属,而且毒性很大,有抑制生物降解的特性,对周围水资源和生态环境有着严重的影响。Petrochemical industry is an industry that uses petroleum, natural gas, etc. as raw materials to process them into various chemical products. Petrochemical wastewater is wastewater discharged from the production process of petrochemical enterprises. The source nodes of sewage are distributed in various production devices, crude oil tank farms, water supply and drainage workshops, etc. There are many kinds of substances in petrochemical wastewater, the composition is complex, and the content of organic matter is high. The COD is about 600~1200mg/L, and the BOD is 200~1000mg/L. It is very toxic and has the property of inhibiting biodegradation, which has a serious impact on the surrounding water resources and ecological environment.

石油化工废水是比较难处理的一类工业废水,具有以下特点:Petrochemical wastewater is a type of industrial wastewater that is difficult to treat, and has the following characteristics:

①水质成分复杂且副产物多,反应原料多为溶剂类物质或环状结构化合物等;①The water quality components are complex and there are many by-products, and the reaction raw materials are mostly solvent substances or ring-structured compounds, etc.;

②废水中污染物浓度高;② High concentration of pollutants in wastewater;

③有毒有害物质多,如卤族化合物、硝基化合物、硫化物、部分表面活性剂或分散剂等;③There are many toxic and harmful substances, such as halogen compounds, nitro compounds, sulfides, some surfactants or dispersants, etc.;

④BOD/COD值低,可生化性差;④ Low BOD/COD value and poor biodegradability;

⑤废水色度高。⑤ High chroma of wastewater.

传统处理工艺在一定程度可以解决这些问题,但是存在二次污染严重、处理后污泥产量大、能耗高、出水水质达不到排放标准等情况。近年来,石油化工企业更加重视炼化一体化的快速发展,逐步将核心产业朝着精细化工方向发展,导致化工企业污水水质越来越复杂,仅仅依靠传统的处理工艺流程很难满足环境保护的要求,难以符合国家污水处理排放的标准。The traditional treatment process can solve these problems to a certain extent, but there are serious secondary pollution, large sludge output after treatment, high energy consumption, and effluent water quality that cannot meet the discharge standards. In recent years, petrochemical companies have paid more attention to the rapid development of refining and chemical integration, and gradually developed their core industries towards fine chemicals, resulting in more and more complex sewage water quality in chemical companies. It is difficult to meet environmental protection requirements only by relying on traditional treatment processes. Requirements, it is difficult to meet the national sewage treatment discharge standards.

此外,抑制生物降解及难生物降解的高浓度废水是石油化工企业废水处理中的主要难点。这部分废水能否得到妥善处理是影响石油化工企业排水达到排放标准的关键。国内外对此都非常重视,通常采用化学或物理方法处理,但并不是所有石化废水均难降解,仅少部分特殊工艺或产品产生废水难于处理或者说难于生化处理,如果来水统一进行化学或物理方法存在运行费用高的问题,且效果较差。本发明针对不同水质状况的原水,采用模块化智能识别控制系统,使污水选择性的进入合理处理单元,降低运行费用,提高处理效率。In addition, high-concentration wastewater that inhibits biodegradation and is difficult to biodegrade is the main difficulty in wastewater treatment in petrochemical enterprises. Whether this part of wastewater can be properly treated is the key to affecting the drainage of petrochemical enterprises to meet the discharge standards. Both at home and abroad attach great importance to this, and usually use chemical or physical methods to treat it, but not all petrochemical wastewater is difficult to degrade, only a small number of special processes or products produce wastewater that is difficult to treat or biochemically. The physical method has the problem of high operating cost and poor effect. Aiming at raw water with different water quality conditions, the invention adopts a modularized intelligent identification control system, so that sewage can be selectively entered into a reasonable treatment unit, thereby reducing operating costs and improving treatment efficiency.

发明内容Contents of the invention

针对现有技术存在的问题,本发明提供一种石油化工工业废水处理集成工艺系统及方法,对石化企业生产过程中产生的各种废水进行工艺集成与参数化设计处理,实现废水处理工艺的模块化、智能化、集成化、高效化。本发明的技术方案为:Aiming at the problems existing in the prior art, the present invention provides an integrated process system and method for petrochemical industrial wastewater treatment, which performs process integration and parametric design treatment for various wastewater generated in the production process of petrochemical enterprises, and realizes the module of wastewater treatment process Smart, intelligent, integrated and efficient. Technical scheme of the present invention is:

一种石油化工工业废水处理集成工艺系统,包括在线监测分析系统、智能反馈控制系统、废水处理系统;所述在线监测分析系统用于对石油化工工业废水的水质成分以及各个处理环节出水的水质成分进行监测分析,并将监测分析数据传送至所述智能反馈控制系统;所述智能反馈控制系统对所述监测分析数据处理后输出控制信号至所述废水处理系统;An integrated process system for petrochemical industrial wastewater treatment, including an online monitoring and analysis system, an intelligent feedback control system, and a wastewater treatment system; Perform monitoring and analysis, and transmit the monitoring and analysis data to the intelligent feedback control system; the intelligent feedback control system outputs control signals to the wastewater treatment system after processing the monitoring and analysis data;

所述废水处理系统包括预处理模块、除油模块、生化模块、污泥处理模块及深度处理模块;所述预处理模块、除油模块、生化模块、深度处理模块及污泥处理模块根据智能反馈控制系统输出的控制信号指令对石油化工工业废水进行处理;The wastewater treatment system includes a pretreatment module, an oil removal module, a biochemical module, a sludge treatment module and an advanced treatment module; the pretreatment module, an oil removal module, a biochemical module, an advanced treatment module and a sludge treatment module are The control signal output by the control system commands the treatment of petrochemical industrial wastewater;

所述预处理模块包括旋流沉砂池和水质调节池,所述旋流沉砂池进口连接石油化工工业废水入口,出口连接所述水质调节池进口;所述水质调节池出口连接所述生化模块进口;The pretreatment module includes a swirl grit chamber and a water quality adjustment tank, the inlet of the swirl grit chamber is connected to the petrochemical industrial wastewater inlet, and the outlet is connected to the inlet of the water quality adjustment tank; the outlet of the water quality adjustment tank is connected to the biochemical module imports;

所述除油模块包括隔油池、高强度纤维过滤池、旋流气浮池、电絮凝系统,所述隔油池进口连接石油化工工业废水入口,出口分别连接所述高强度纤维过滤池、所述旋流气浮池、所述电絮凝系统进口;所述高强度纤维过滤池、所述旋流气浮池、所述电絮凝系统出水口连接所述生化模块进口;所述高强度纤维过滤池、所述旋流气浮池、所述电絮凝系统污泥出口连接所述污泥处理模块进口;The degreasing module includes a grease trap, a high-strength fiber filter pool, a swirling air flotation pool, and an electroflocculation system. The inlet of the grease trap is connected to the petrochemical industry wastewater inlet, and the outlet is respectively connected to the high-strength fiber filter pool, the The swirl air flotation pool and the inlet of the electrocoagulation system; the high-strength fiber filter pool, the swirl air flotation pool, and the outlet of the electrocoagulation system are connected to the inlet of the biochemical module; the high-strength fiber filter pool, the cyclone The flow air floating tank and the sludge outlet of the electrocoagulation system are connected to the inlet of the sludge treatment module;

所述生化模块分成两部分,一部分包括水解酸化罐,另一部分包括芬顿氧化罐,所述水解酸化罐或所述芬顿氧化罐出口与高效好氧生物反应器或间歇式生物膜反应器进口连接;所述高效好氧生物反应器或所述间歇式生物膜反应器出水口连接所述深度处理模块进口;所述高效好氧生物反应器或所述间歇式生物膜反应器污泥出口连接所述污泥处理模块进口;The biochemical module is divided into two parts, one part includes a hydrolysis acidification tank, the other part includes a Fenton oxidation tank, the outlet of the hydrolysis acidification tank or the Fenton oxidation tank is connected to the inlet of a high-efficiency aerobic bioreactor or a batch biofilm reactor Connection; the outlet of the high-efficiency aerobic bioreactor or the batch biofilm reactor is connected to the inlet of the advanced treatment module; the outlet of the high-efficiency aerobic bioreactor or the batch biofilm reactor sludge is connected The inlet of the sludge treatment module;

所述污泥处理模块包括依次连接的污泥回收贮存池、浓缩池和板框压滤池,所述板框压滤池出水口连接所述高效好氧生物反应器或所述间歇式生物膜反应器进口;The sludge treatment module includes a sludge recovery storage tank, a thickening tank, and a plate-and-frame filter press tank connected in sequence, and the outlet of the plate-and-frame filter press tank is connected to the high-efficiency aerobic bioreactor or the intermittent biofilm Reactor inlet;

所述深度处理模块分成两部分,一部分包括臭氧活性炭吸附池,另一部分包括依次连接的超滤膜过滤池和反渗透池。The advanced treatment module is divided into two parts, one part includes an ozone activated carbon adsorption pool, and the other part includes an ultrafiltration membrane filter pool and a reverse osmosis pool connected in sequence.

进一步地,所述预处理模块还设有酸碱调节系统,所述酸碱调节系统连接所述水质调节池。Further, the pretreatment module is also provided with an acid-base adjustment system, and the acid-base adjustment system is connected to the water quality adjustment pool.

进一步地,所述预处理模块还设有洗砂池,所述洗砂池进砂口连接所述旋流沉砂池,出水口连接所述水质调节池。Further, the pretreatment module is also provided with a sand washing tank, the sand inlet of the sand washing tank is connected to the swirl grit chamber, and the water outlet is connected to the water quality adjustment tank.

进一步地,所述除油模块还设有有机高分子絮凝剂投加系统,所述有机高分子絮凝剂投加系统连接所述旋流气浮池。Further, the degreasing module is also provided with an organic polymer flocculant dosing system, and the organic polymer flocculant dosing system is connected to the cyclone air flotation tank.

进一步地,所述水解酸化罐或所述芬顿氧化罐与所述高效好氧生物反应器或所述间歇式生物膜反应器的连接管路上设有三通控制阀。Further, a three-way control valve is provided on the connecting pipeline between the hydrolysis acidification tank or the Fenton oxidation tank and the high-efficiency aerobic bioreactor or the batch biofilm reactor.

进一步地,所述生化模块还设有生物工程菌剂投加系统,所述生物工程菌剂投加系统连接所述高效好氧生物反应器。Further, the biochemical module is also provided with a bioengineering bacterial agent dosing system connected to the high-efficiency aerobic bioreactor.

一种石油化工工业废水处理集成工艺方法,是采用上述系统,包括以下步骤:An integrated process method for petrochemical industry wastewater treatment, which adopts the above-mentioned system, and includes the following steps:

步骤一,在线监测分析石油化工工业废水的石油类物质浓度,当石油类物质浓度≤50mg/L时进入步骤二,否则进入步骤三;Step 1, online monitoring and analysis of the concentration of petroleum substances in petrochemical industrial wastewater, when the concentration of petroleum substances is less than or equal to 50mg/L, enter step 2, otherwise enter step 3;

步骤二,启动运行预处理模块,将石油化工工业废水引入旋流沉砂池沉沙,监测沉沙后废水pH值,并将沉沙后废水引入水质调节池,当pH>8.5或pH<6.5时,在水质调节池投加酸或碱调节至6.5≤pH≤8.5,否则直接进入步骤四;Step 2: start and run the pretreatment module, introduce the petrochemical industry wastewater into the cyclone grit chamber for sand deposition, monitor the pH value of the wastewater after sedimentation, and introduce the wastewater after sedimentation into the water quality adjustment tank, when the pH>8.5 or pH<6.5 , add acid or alkali to the water quality adjustment tank to adjust to 6.5≤pH≤8.5, otherwise go directly to step 4;

步骤三,启动运行除油模块,将石油化工工业废水引入隔油池进行初次油水分离,监测初次油水分离后废水中粒径在0.1~10μm油类颗粒的质量百分比,当粒径在0.1~10μm油类颗粒的质量百分比>50%时,初次油水分离的废水进入旋流气浮池进行二次油水分离;当粒径在0.1~10μm油类颗粒的质量百分比≤50%且在所述油类颗粒中粒径<0.1μm的溶解油质量百分比>30%时,初次油水分离的废水进入电絮凝系统进行二次油水分离,否则初次油水分离的废水进入高强度纤维过滤池进行二次油水分离;所有二次油水分离后的泥渣进入步骤六,所有二次油水分离后的废水进入步骤四;Step 3: start and run the degreasing module, introduce petrochemical industrial wastewater into the grease trap for initial oil-water separation, monitor the mass percentage of oil particles with a particle size of 0.1-10 μm in the wastewater after the initial oil-water separation, and when the particle size is 0.1-10 μm When the mass percentage of oil particles > 50%, the wastewater from the primary oil-water separation enters the cyclone air flotation tank for secondary oil-water separation; when the mass percentage of oil particles with a particle size of 0.1-10 μm When the mass percentage of dissolved oil with a particle size of <0.1 μm is >30%, the wastewater from the primary oil-water separation enters the electroflocculation system for secondary oil-water separation, otherwise the wastewater from the primary oil-water separation enters the high-strength fiber filter tank for secondary oil-water separation; all secondary The sludge after the primary oil-water separation enters step six, and all the waste water after the secondary oil-water separation enters step four;

步骤四,启动运行生化模块,监测生化模块进口处废水BOD5/COD值,将BOD5/COD<0.1的废水引入芬顿氧化罐处理,否则引入水解酸化罐处理,监测芬顿氧化罐或水解酸化罐出口处废水的TN浓度;Step 4: Start the biochemical module, monitor the BOD 5 /COD value of the wastewater at the inlet of the biochemical module, introduce the wastewater with BOD 5 /COD<0.1 into the Fenton oxidation tank for treatment, otherwise introduce the hydrolysis acidification tank for treatment, monitor the Fenton oxidation tank or hydrolysis TN concentration of wastewater at the outlet of the acidification tank;

步骤五,将TN浓度>50mg/L的废水引入间歇式生物膜反应器,否则引入高效好氧生物反应器;从间歇式生物膜反应器或高效好氧生物反应器出来的污泥进入步骤六,从间歇式生物膜反应器或高效好氧生物反应器出来的废水进入步骤七;Step five, introduce wastewater with TN concentration > 50mg/L into batch biofilm reactor, otherwise introduce high-efficiency aerobic bioreactor; sludge from batch biofilm reactor or high-efficiency aerobic bioreactor enters step six , the wastewater from the batch biofilm reactor or high-efficiency aerobic bioreactor enters step seven;

步骤六,启动污泥处理模块,将污泥依次引入污泥回收贮存池、浓缩池和板框压滤池进行无害化脱水处理,脱水后的泥饼外运,污泥浓缩液监测TN浓度后重复步骤五~步骤六;Step 6: Start the sludge treatment module, introduce the sludge into the sludge recovery storage tank, the concentration tank and the plate and frame filter tank in sequence for harmless dehydration treatment, and transport the dehydrated mud cake outside, and monitor the concentration of TN in the sludge concentrate Then repeat steps five to six;

步骤七,启动深度处理模块,监测深度处理模块进口处废水的色度,将色度>200且SS浓度>50mg/L的废水依次引入超滤膜过滤池和反渗透池处理,否则引入臭氧活性炭吸附池处理。Step 7: Start the advanced treatment module, monitor the chromaticity of the wastewater at the inlet of the advanced treatment module, and introduce the wastewater with a chromaticity > 200 and a SS concentration > 50mg/L into the ultrafiltration membrane filter pool and reverse osmosis pool for treatment, otherwise introduce ozone activated carbon Adsorption pool treatment.

上述方法中,所述步骤二的将废水引入旋流沉砂池沉沙,还包括将分离后的沉沙清洗,清洗水引入水质调节池进行后续处理。In the above method, the step 2 of introducing waste water into a cyclone grit chamber for sand deposition also includes washing the separated sand, and introducing the cleaning water into a water quality adjustment tank for subsequent treatment.

上述方法中,所述步骤四的水解酸化罐的运行参数为:反应温度22~25℃,水力停留时间5~6h,污泥停留时间2.5~3d,COD容积负荷10~16kg/(m3﹒d)。In the above method, the operating parameters of the hydrolysis acidification tank in step 4 are: reaction temperature 22-25°C, hydraulic retention time 5-6h, sludge retention time 2.5-3d, COD volume load 10-16kg/(m 3 . d).

上述方法中,所述步骤七的臭氧活性炭吸附池的运行参数为:通臭氧时间3~5min,臭氧通氧量120~140mg/L,活性炭吸附时间10~15min,炭柱直径2~2.5m,炭层高度2.5~3.0m,总停留时间25~30min,臭氧与从生化处理模块出来的废水的流量比(3.5~4.0):1。In the above method, the operating parameters of the ozone activated carbon adsorption pool in the step 7 are: the ozone passing time is 3~5min, the ozone oxygen passing rate is 120~140mg/L, the activated carbon adsorption time is 10~15min, and the carbon column diameter is 2~2.5m. The height of the carbon layer is 2.5~3.0m, the total residence time is 25~30min, and the flow ratio of ozone to wastewater from the biochemical treatment module (3.5~4.0):1.

本发明的有益效果是:本发明可针对不同性质的石油化工工业废水的特点和处理难点,灵活启用高效、稳定的处理工艺组合,以实现处理过程的优化配置,集成化、智能化、模块化程度高;经本发明处理后的石油化工工业废水的SS、COD、色度等指标稳定达标,出水可再生利用;此外,本发明有利于技术与集成设备的相互转化,还能有效节省石油化工工业废水的处理空间,工艺运行可靠,具有较高的工业化价值。The beneficial effects of the present invention are: the present invention can flexibly use efficient and stable treatment process combinations for the characteristics and treatment difficulties of different types of petrochemical industrial wastewater, so as to realize the optimal configuration of the treatment process, integration, intelligence and modularization The degree is high; the SS, COD, chroma and other indicators of the petrochemical industrial wastewater treated by the present invention are stable up to the standard, and the effluent can be recycled; in addition, the present invention is conducive to the mutual conversion of technology and integrated equipment, and can effectively save petrochemical industry waste. The treatment space for industrial waste water has reliable process operation and high industrial value.

附图说明Description of drawings

图1是本发明的石油化工工业废水处理集成工艺系统的一种结构示意图,其中a、多参数全自动水质检测分析仪,b、PLC可编程逻辑控制器,c、预处理模块,e、除油模块,d、生化模块,g、深度处理模块,f、污泥处理模块;1-旋流沉砂池、2-水质调节池、3-水解酸化罐、4-芬顿氧化罐、5-高效好氧生物反应器、6-间歇式生物膜反应器、7-臭氧活性炭吸附池、8-超滤膜过滤池UF、9-反渗透池、10-隔油池、11-洗砂池、12-高强度纤维过滤池、13-旋流气浮池、14-有机高分子絮凝剂投机系统、15-电絮凝系统、16-污泥回收贮存池、17-浓缩池、18-板框压滤池、19-酸碱调节系统、20-生物工程菌剂投加系统。Fig. 1 is a kind of structural representation of petrochemical industrial wastewater treatment integrated process system of the present invention, wherein a, multi-parameter automatic water quality detection analyzer, b, PLC programmable logic controller, c, pretreatment module, e, except Oil module, d, biochemical module, g, advanced treatment module, f, sludge treatment module; 1-cyclone grit chamber, 2-water quality adjustment tank, 3-hydrolysis acidification tank, 4-Fenton oxidation tank, 5- High-efficiency aerobic bioreactor, 6-batch biofilm reactor, 7-ozone activated carbon adsorption tank, 8-ultrafiltration membrane filter UF, 9-reverse osmosis tank, 10-grease trap, 11-sand washing tank, 12-High-strength fiber filter tank, 13-Swirl air flotation tank, 14-Organic polymer flocculant speculative system, 15-Electric flocculation system, 16-Sludge recovery storage tank, 17-Concentration tank, 18-Plate and frame filter tank , 19-acid-base adjustment system, 20-biological engineering bacteria agent dosing system.

具体实施方式detailed description

下面结合附图和具体的实施例对本发明做进一步详细说明,所述是对本发明的解释而不是限定。The present invention will be described in further detail below in conjunction with the accompanying drawings and specific embodiments, which are explanations rather than limitations of the present invention.

本发明提供了一种石油化工工业废水处理集成工艺系统,其结构如图1所示,包括在线监测分析系统、智能反馈控制系统、废水处理系统,所述在线监测分析系统具体为多参数全自动水质检测分析仪a,用于对石油化工工业废水的水质成分以及各个处理环节出水的水质成分进行监测分析,并将监测分析数据传送至所述智能反馈控制系统;所述智能反馈控制系统具体为PLC可编程逻辑控制器b,用于对所述监测分析数据处理后输出控制信号至所述废水处理系统。The present invention provides an integrated process system for petrochemical industrial wastewater treatment. Its structure is shown in Figure 1, including an online monitoring and analysis system, an intelligent feedback control system, and a wastewater treatment system. The online monitoring and analysis system is specifically a multi-parameter fully automatic The water quality detection analyzer a is used to monitor and analyze the water quality components of the petrochemical industrial wastewater and the water quality components of the effluent from each treatment link, and transmit the monitoring and analysis data to the intelligent feedback control system; the intelligent feedback control system is specifically The PLC programmable logic controller b is used to output control signals to the wastewater treatment system after processing the monitoring and analysis data.

所述废水处理系统包括预处理模块c、除油模块e、生化模块d、污泥处理模块f及深度处理模块g;所述预处理模块c、除油模块e、生化模块d、深度处理模块g及污泥处理模块f根据PLC可编程逻辑控制器b输出的控制信号指令对石油化工工业废水进行处理。The wastewater treatment system includes a pretreatment module c, an oil removal module e, a biochemical module d, a sludge treatment module f, and an advanced treatment module g; the pretreatment module c, an oil removal module e, a biochemical module d, and an advanced treatment module g and the sludge treatment module f process petrochemical industrial wastewater according to the control signal instructions output by the PLC programmable logic controller b.

所述预处理模块c包括旋流沉砂池1和水质调节池2,所述旋流沉砂池1进口连接石油化工工业废水入口,出口连接所述水质调节池2进口;所述水质调节池2出口连接所述生化模块d进口;所述预处理模块c还设有酸碱调节系统19和洗砂池11,所述酸碱调节系统19连接所述水质调节池2,所述酸碱调节系统19用于控制生石灰或硫酸的投加,来调节水质调节池中的pH值;所述洗砂池11进砂口连接所述旋流沉砂池1,出水口连接所述水质调节池2。The pretreatment module c includes a swirl grit chamber 1 and a water quality adjustment pond 2, the inlet of the swirl grit chamber 1 is connected to the petrochemical industrial wastewater inlet, and the outlet is connected to the inlet of the water quality adjustment pond 2; the water quality adjustment pond 2 The outlet is connected to the import of the biochemical module d; the pretreatment module c is also provided with an acid-base adjustment system 19 and a sand washing tank 11, the acid-base adjustment system 19 is connected to the water quality adjustment pool 2, and the acid-base adjustment system System 19 is used to control the dosing of quicklime or sulfuric acid to adjust the pH value in the water quality adjustment tank; the sand inlet of the sand washing tank 11 is connected to the cyclone grit chamber 1, and the water outlet is connected to the water quality adjustment tank 2 .

所述除油模块e包括隔油池10、高强度纤维过滤池12、旋流气浮池13、电絮凝系统15,所述隔油池10进口连接石油化工工业废水入口,出口分别连接所述高强度纤维过滤池12、所述旋流气浮池13、所述电絮凝系统15进口;所述高强度纤维过滤池12、所述旋流气浮池13、所述电絮凝系统15出水口连接所述生化模块d进口;所述高强度纤维过滤池12、所述旋流气浮池13、所述电絮凝系统15污泥出口连接所述污泥处理模块f进口;所述除油模块e还设有有机高分子絮凝剂投加系统14,所述有机高分子絮凝剂投加系统14连接所述旋流气浮池13,所述有机高分子絮凝剂投加系统14用于控制有机高分子絮凝剂投加至所述旋流气浮池13中。The degreasing module e includes a grease trap 10, a high-strength fiber filter pool 12, a swirling air flotation tank 13, and an electroflocculation system 15. The inlet of the grease trap 10 is connected to the petrochemical industrial wastewater inlet, and the outlet is connected to the high-strength fiber filter respectively. The fiber filter pool 12, the swirl air flotation pool 13, and the inlet of the electrocoagulation system 15; the high-strength fiber filter pool 12, the swirl air flotation pool 13, and the electrocoagulation system 15 outlet are connected to the biochemical module d Import; the high-strength fiber filter tank 12, the swirling air flotation tank 13, and the sludge outlet of the electrocoagulation system 15 are connected to the inlet of the sludge treatment module f; the degreasing module e is also provided with organic polymer flocculation agent dosing system 14, the organic polymer flocculant dosing system 14 is connected to the cyclone air flotation tank 13, the organic polymer flocculant dosing system 14 is used to control the addition of organic polymer flocculant to the cyclone In the air flow floating pool 13.

所述生化模块d分成两部分,一部分包括水解酸化罐3,另一部分包括芬顿氧化罐4,所述水解酸化罐3或所述芬顿氧化罐4出口与高效好氧生物反应器5或间歇式生物膜反应器6进口连接;所述高效好氧生物反应器5或所述间歇式生物膜反应器6出水口连接所述深度处理模块g进口;所述高效好氧生物反应器5或所述间歇式生物膜反应器6污泥出口连接所述污泥处理模块f进口;所述水解酸化罐3或所述芬顿氧化罐4与所述高效好氧生物反应器5或所述间歇式生物膜反应器6的连接管路上设有三通控制阀;所述生化模块d还设有生物工程菌剂投加系统20,所述生物工程菌剂投加系统20连接所述高效好氧生物反应器5,所述生物工程菌剂投加系统20用于控制生物菌剂投加至所述高效好氧生物反应器5中。The biochemical module d is divided into two parts, one part includes a hydrolysis acidification tank 3, and the other part includes a Fenton oxidation tank 4, and the outlet of the hydrolysis acidification tank 3 or the Fenton oxidation tank 4 is connected to a high-efficiency aerobic bioreactor 5 or intermittent Type biofilm reactor 6 inlet connection; The high-efficiency aerobic bioreactor 5 or the intermittent biofilm reactor 6 water outlet is connected to the advanced treatment module g inlet; The high-efficiency aerobic bioreactor 5 or the The sludge outlet of the batch biofilm reactor 6 is connected to the inlet of the sludge treatment module f; The connecting pipeline of the biofilm reactor 6 is provided with a three-way control valve; the biochemical module d is also provided with a bioengineering bacterial agent dosing system 20, and the bioengineering bacterial agent dosing system 20 is connected to the high-efficiency aerobic biological reaction device 5, the bioengineering bacterial agent dosing system 20 is used to control the feeding of biological bacterial agents into the high-efficiency aerobic bioreactor 5.

所述污泥处理模块f包括依次连接的污泥回收贮存池16、浓缩池17和板框压滤池18,所述板框压滤池18出水口连接所述高效好氧生物反应器5或所述间歇式生物膜反应器6进口.The sludge treatment module f includes a sludge recovery storage tank 16, a thickening tank 17 and a plate and frame filter press tank 18 connected in sequence, and the outlet of the plate and frame filter press tank 18 is connected to the high-efficiency aerobic bioreactor 5 or The 6 inlets of the batch biofilm reactor.

所述深度处理模块g分成两部分,一部分包括臭氧活性炭吸附池7,另一部分包括依次连接的超滤膜过滤池8和反渗透池9,经返渗透池出来的水为SS、COD、色度等指标稳定达标的合格水。The advanced treatment module g is divided into two parts, one part includes an ozone activated carbon adsorption tank 7, and the other part includes an ultrafiltration membrane filter tank 8 and a reverse osmosis tank 9 connected in sequence, and the water that comes out of the reverse osmosis tank is SS, COD, chroma Qualified water with stable and up-to-standard indicators.

本发明还提供一种石油化工工业废水处理集成工艺方法,是采用上述系统,包括以下步骤:The present invention also provides an integrated process method for petrochemical industrial wastewater treatment, which adopts the above-mentioned system and includes the following steps:

步骤一,在线监测分析石油化工工业废水的石油类物质浓度,当石油类物质浓度≤50mg/L时进入步骤二,否则进入步骤三;Step 1, online monitoring and analysis of the concentration of petroleum substances in petrochemical industrial wastewater, when the concentration of petroleum substances is less than or equal to 50mg/L, enter step 2, otherwise enter step 3;

步骤二,启动运行预处理模块,将石油化工工业废水引入旋流沉砂池沉沙,将分离后的沉沙清洗,监测沉沙后废水pH值,并将沉沙后废水和沉沙清洗水合并后引入水质调节池,当pH>8.5或pH<6.5时,在水质调节池投加酸或碱调节至6.5≤pH≤8.5,否则直接进入步骤四;Step 2: start and run the pretreatment module, introduce the petrochemical industrial wastewater into the cyclone grit chamber for sand deposition, wash the separated sand, monitor the pH value of the wastewater after sedimentation, and transfer the wastewater and cleaning water after sedimentation After merging, it is introduced into the water quality adjustment tank. When the pH>8.5 or pH<6.5, add acid or alkali to the water quality adjustment tank to adjust to 6.5≤pH≤8.5, otherwise directly go to step 4;

步骤三,启动运行除油模块,将石油化工工业废水引入隔油池进行初次油水分离,监测初次油水分离后废水中粒径在0.1~10μm油类颗粒的质量百分比,当粒径在0.1~10μm油类颗粒的质量百分比>50%时,初次油水分离的废水进入旋流气浮池进行二次油水分离;当粒径在0.1~10μm油类颗粒的质量百分比≤50%且在所述油类颗粒中粒径<0.1μm的溶解油质量百分比>30%时,初次油水分离的废水进入电絮凝系统进行二次油水分离,否则初次油水分离的废水进入高强度纤维过滤池进行二次油水分离;所有二次油水分离后的泥渣进入步骤六,所有二次油水分离后的废水进入步骤四;Step 3: start and run the degreasing module, introduce petrochemical industrial wastewater into the grease trap for initial oil-water separation, monitor the mass percentage of oil particles with a particle size of 0.1-10 μm in the wastewater after the initial oil-water separation, and when the particle size is 0.1-10 μm When the mass percentage of oil particles > 50%, the wastewater from the primary oil-water separation enters the cyclone air flotation tank for secondary oil-water separation; when the mass percentage of oil particles with a particle size of 0.1-10 μm When the mass percentage of dissolved oil with a particle size of <0.1 μm is >30%, the wastewater from the primary oil-water separation enters the electroflocculation system for secondary oil-water separation, otherwise the wastewater from the primary oil-water separation enters the high-strength fiber filter tank for secondary oil-water separation; all secondary The sludge after the primary oil-water separation enters step six, and all the waste water after the secondary oil-water separation enters step four;

步骤四,启动运行生化模块,监测生化模块进口处废水BOD5/COD值,将BOD5/COD<0.1的废水引入芬顿氧化罐处理,否则引入水解酸化罐处理,监测芬顿氧化罐或水解酸化罐出口处废水的TN浓度;其中水解酸化罐的运行参数为:反应温度22~25℃,水力停留时间5~6h,污泥停留时间2.5~3d,COD容积负荷10~16kg/(m3﹒d);Step 4: Start the biochemical module, monitor the BOD 5 /COD value of the wastewater at the inlet of the biochemical module, introduce the wastewater with BOD 5 /COD<0.1 into the Fenton oxidation tank for treatment, otherwise introduce the hydrolysis acidification tank for treatment, monitor the Fenton oxidation tank or hydrolysis The TN concentration of the wastewater at the outlet of the acidification tank; the operating parameters of the hydrolysis acidification tank are: reaction temperature 22~25℃, hydraulic retention time 5~6h, sludge residence time 2.5~3d, COD volume load 10~16kg/(m 3 .d);

步骤五,将TN浓度>50mg/L的废水引入间歇式生物膜反应器,否则引入高效好氧生物反应器;从间歇式生物膜反应器或高效好氧生物反应器出来的污泥进入步骤六,从间歇式生物膜反应器或高效好氧生物反应器出来的废水进入步骤七;Step five, introduce wastewater with TN concentration > 50mg/L into batch biofilm reactor, otherwise introduce high-efficiency aerobic bioreactor; sludge from batch biofilm reactor or high-efficiency aerobic bioreactor enters step six , the wastewater from the batch biofilm reactor or high-efficiency aerobic bioreactor enters step seven;

步骤六,启动污泥处理模块,将污泥依次引入污泥回收贮存池、浓缩池和板框压滤池进行无害化脱水处理,脱水后的泥饼外运,污泥浓缩液监测TN浓度后重复步骤五~步骤六;Step 6: Start the sludge treatment module, introduce the sludge into the sludge recovery storage tank, the concentration tank and the plate and frame filter tank in sequence for harmless dehydration treatment, and transport the dehydrated mud cake outside, and monitor the concentration of TN in the sludge concentrate Then repeat steps five to six;

步骤七,启动深度处理模块,监测深度处理模块进口处废水的色度,将色度>200且SS浓度>50mg/L的废水依次引入超滤膜过滤池和反渗透池处理,否则引入臭氧活性炭吸附池处理;其中臭氧活性炭吸附池的运行参数为:通臭氧时间3~5min,臭氧通氧量120~140mg/L,活性炭吸附时间10~15min,炭柱直径2~2.5m,炭层高度2.5~3.0m,总停留时间25~30min,臭氧与从生化处理模块出来的废水的流量比(3.5~4.0):1;处理完毕的水SS、COD、色度等指标稳定达标。Step 7: Start the advanced treatment module, monitor the chromaticity of the wastewater at the inlet of the advanced treatment module, and introduce the wastewater with a chromaticity > 200 and a SS concentration > 50mg/L into the ultrafiltration membrane filter pool and reverse osmosis pool for treatment, otherwise introduce ozone activated carbon Adsorption pool treatment; the operating parameters of the ozone activated carbon adsorption pool are: ozone passage time 3~5min, ozone oxygen flux 120~140mg/L, activated carbon adsorption time 10~15min, carbon column diameter 2~2.5m, carbon layer height 2.5 ~3.0m, the total residence time is 25~30min, the flow rate ratio of ozone to wastewater from the biochemical treatment module (3.5~4.0): 1; the SS, COD, chroma and other indicators of the treated water are stably up to standard.

本发明对不同水质来源的石油化工废水进行集成处理,处理结果如下:The present invention performs integrated treatment on petrochemical wastewater from different water quality sources, and the treatment results are as follows:

实施例1Example 1

石油化甲工厂废水水质如下表1:The wastewater quality of petrochemical plant A is as follows in Table 1:

表1石油化甲工厂废水水质Table 1 Wastewater quality of petrochemical plant A

水质参数Water Quality Parameters 石油类Petro CODCOD TNTN 色度(稀释倍数)Chroma (dilution factor) pHpH SSSS 氯化物chloride 浓度/(mg/L)Concentration/(mg/L) 32.632.6 1545.51545.5 456.5456.5 0.2950.295 6060 346346 8.88.8 7676 24.424.4

表2 废水中石油类粒径占比Table 2 The proportion of petroleum particle size in wastewater

油脂类型grease type 浮油oil slick 分散油Disperse oil 乳化油emulsified oil 溶解油dissolved oil 粒径μmParticle size μm >100>100 10~10010~100 0.1~100.1~10 <0.1<0.1 百分比%percentage% 2020 1010 5555 1515

启动在线监测分析系统多参数全自动水质检测分析仪对进入系统的石油化工废水和各控制节点的水质进行监测分析,分析石油化工废水水质成分,根据成分参数,PLC可编程逻辑控制器选择废水处理系统的具体启动模块,具体是:Start the online monitoring and analysis system with a multi-parameter automatic water quality detection analyzer to monitor and analyze the petrochemical wastewater entering the system and the water quality of each control node, analyze the water quality components of the petrochemical wastewater, and select the wastewater treatment according to the composition parameters. The specific startup modules of the system are:

监测石油化工废水进水石油类物质浓度=32.6≤50 mg/L,废水进入旋流沉砂池;Monitor the concentration of petroleum substances in the petrochemical wastewater influent = 32.6≤50 mg/L, and the wastewater enters the cyclone grit chamber;

监测水质调节池内废水pH=8.8>8.5,酸碱调节系统投加硫酸调节直至6.5≤pH≤8.5;Monitor the pH of the wastewater in the water quality adjustment pool = 8.8 > 8.5, and add sulfuric acid to the acid-base adjustment system to adjust until 6.5≤pH≤8.5;

监测进入生化模块的混合废水BOD5/COD=0.295>0.1,废水进入水解酸化罐,水解酸化反应器的运行参数:T=25℃、水力停留时间(HRT)=5.5h、污泥停留时间(SRT)=2.75d、COD容积负荷13kg/(m3﹒d);Monitor the mixed wastewater entering the biochemical module BOD 5 /COD=0.295>0.1, the wastewater enters the hydrolysis acidification tank, the operating parameters of the hydrolysis acidification reactor: T=25°C, hydraulic retention time (HRT)=5.5h, sludge retention time ( SRT)=2.75d, COD volume load 13kg/(m 3 ﹒d);

监测水解酸化罐出口处的混合废水TN浓度=60>50mg/L,废水进入间歇式生物膜反应器;Monitor the mixed wastewater TN concentration at the outlet of the hydrolysis acidification tank=60>50mg/L, and the wastewater enters the batch biofilm reactor;

监测进入深度处理模块的混合废水色度(稀释倍数法)=346>200,且SS=76>50mg/L,废水进入超滤膜过滤池UF和反渗透RO。Monitor the color of the mixed wastewater entering the advanced treatment module (dilution multiple method) = 346 > 200, and SS = 76 > 50mg/L, and the wastewater enters the ultrafiltration membrane filter pool UF and reverse osmosis RO.

经过本实施例的集成工艺系统处理后的废水,其中石油类物质浓度为7mg/L,COD浓度为35~55mg/L,SS浓度为8~13mg/L,TN浓度10~15mg/L,色度(稀释倍数)为10~19,石油类、COD、SS、TN和色度(稀释倍数)的平均去除率分别为82~94%、91~96%、71~82%、90~95%和93~98%。Wastewater treated by the integrated process system of this embodiment, wherein the concentration of petroleum substances is 7mg/L, the concentration of COD is 35~55mg/L, the concentration of SS is 8~13mg/L, and the concentration of TN is 10~15mg/L. The degree (dilution multiple) is 10~19, and the average removal rates of petroleum, COD, SS, TN and chroma (dilution multiple) are 82~94%, 91~96%, 71~82%, 90~95% respectively and 93~98%.

实施例2Example 2

石油化乙厂废水水质如下表3:The wastewater quality of petrochemical plant B is shown in Table 3:

表3石油化乙工厂废水水质Table 3 Wastewater quality of petrochemical plant B

水质参数Water Quality Parameters 石油类Petro CODCOD TNTN 色度(稀释倍数)Chroma (dilution factor) pHpH SSSS 氯化物chloride 浓度/(mg/L)Concentration/(mg/L) 58.458.4 523.5523.5 134.5134.5 0.2570.257 4545 245245 7.57.5 5555 14.814.8

表4 废水中石油类粒径占比Table 4 The proportion of petroleum particle size in wastewater

油脂类型grease type 浮油oil slick 分散油Disperse oil 乳化油emulsified oil 溶解油dissolved oil 粒径μmParticle size μm >100>100 10~10010~100 0.1~100.1~10 <0.1<0.1 百分比%percentage% 7070 1010 1515 55

启动在线监测分析系统多参数全自动水质检测分析仪对进入系统的石油化工废水和各控制节点的水质进行监测分析,分析石油化工废水水质成分,根据成分参数,PLC可编程逻辑控制器选择废水处理系统的具体启动模块,具体是:Start the online monitoring and analysis system with a multi-parameter automatic water quality detection analyzer to monitor and analyze the petrochemical wastewater entering the system and the water quality of each control node, analyze the water quality components of the petrochemical wastewater, and according to the composition parameters, the PLC programmable logic controller selects wastewater treatment The specific startup modules of the system are:

监测石油化工废水进水石油类物质浓度=58.4>50 mg/L,启动运行除油模块,废水进入隔油池;监测隔油池出水中乳化油(油类粒径0.1~10μm)占比15%<50%、且溶解油(油类粒径<0.1μm)占比5<30%,废水进入高强度纤维过滤池;Monitor the concentration of petroleum substances in the petrochemical wastewater influent = 58.4 > 50 mg/L, start the degreasing module, and the wastewater enters the grease trap; monitor the emulsified oil (oil particle size 0.1~10μm) in the effluent of the grease trap accounting for 15% %<50%, and dissolved oil (oil particle size<0.1μm) accounts for 5<30%, the wastewater enters the high-strength fiber filter pool;

监测进入生化模块的混合废水BOD5/COD=0.25>0.1,废水进入水解酸化罐,水解酸化反应器的运行参数:T=25℃、水力停留时间(HRT)=5h、污泥停留时间(SRT)=2.5d、COD容积负荷10kg/(m3﹒d);Monitor the mixed wastewater entering the biochemical module BOD 5 /COD=0.25>0.1, the wastewater enters the hydrolysis acidification tank, the operating parameters of the hydrolysis acidification reactor: T=25°C, hydraulic retention time (HRT)=5h, sludge retention time (SRT )=2.5d, COD volume load 10kg/(m 3 ﹒d);

监测水解酸化罐出口处的混合废水TN浓度=45<50mg/L,废水进入高效好氧生物反应器;Monitor the mixed wastewater TN concentration at the outlet of the hydrolysis acidification tank = 45<50mg/L, and the wastewater enters the high-efficiency aerobic bioreactor;

监测进入深度处理模块的混合废水色度(稀释倍数法)=240>200,且SS>50mg/L,废水进入超滤膜过滤池和反渗透。Monitor the color of the mixed wastewater entering the advanced treatment module (dilution multiple method) = 240 > 200, and SS > 50mg/L, and the wastewater enters the ultrafiltration membrane filter pool and reverse osmosis.

经过本实施例的集成工艺系统处理后的废水,其中石油类物质浓度为5mg/L, COD浓度为30~50mg/L,SS浓度为5~10mg/L,TN浓度5~15mg/L,色度(稀释倍数)为5~9,石油类、COD、SS、TN和色度(稀释倍数)的平均去除率分别为80~95%、90~95%、75~86%、92~99%和94~98%。Wastewater treated by the integrated process system of this embodiment, wherein the concentration of petroleum substances is 5mg/L, the concentration of COD is 30~50mg/L, the concentration of SS is 5~10mg/L, and the concentration of TN is 5~15mg/L. The degree (dilution multiple) is 5~9, and the average removal rates of petroleum, COD, SS, TN and chroma (dilution multiple) are 80~95%, 90~95%, 75~86%, 92~99% respectively and 94~98%.

应当理解的是,对本领域普通技术人员而言,可以根据上述说明加以改进或变换,而所有这些改进和变换都应落入本发明要求的保护范围内。It should be understood that those skilled in the art can make improvements or changes based on the above description, and all these improvements and changes should fall within the protection scope of the present invention.

Claims (10)

1. a kind of petrochemical industry wastewater treatment integrated technique system, it is characterised in that including online monitoring analysis system, intelligence Can feedback control system, Waste Water Treatment;The on-line monitoring analysis system is used for the water quality to petrochemical industry waste water Composition and the water-quality constituents of each processing links water outlet are monitored analysis, and monitoring analyze data is sent into the intelligence Feedback control system;The Intelligence Feedback control system is described useless to being output control signals to after the monitoring analyze data treatment Water treatment system;
The Waste Water Treatment includes pretreatment module, oil removing module, biochemical module, Treatment of Sludge module and advanced treating mould Block;The pretreatment module, oil removing module, biochemical module, advanced treating module and Treatment of Sludge module are according to Intelligence Feedback control The control signal instruction of system output processed is processed petrochemical industry waste water;
The pretreatment module includes rotational flow grit chamber and water quality adjustment pond, and the rotational flow grit chamber import connects petrochemical industry work Industry waterwater entrance, outlet connection water quality adjustment pond import;The water quality adjustment pond outlet connection biochemical module import;
The oil removing module includes oil interceptor, high strength fibre filtering ponds, cyclone air-flotation pond, electric flocculation system, the oil interceptor Import connect petrochemical industry waterwater entrance, outlet connect respectively the high strength fibre filtering ponds, the cyclone air-flotation pond, The electric flocculation system inlets;The high strength fibre filtering ponds, the cyclone air-flotation pond, the electric flocculation system delivery port connect Connect the biochemical module import;The high strength fibre filtering ponds, the cyclone air-flotation pond, electric flocculation system sludge outlet Connect the Treatment of Sludge module inlet;
The biochemical module is divided into two parts, and a part includes hydrolization and acidification tank, and another part includes Fenton oxidation tank, the water Solution souring tank or Fenton oxidation tank outlet are connected with highly effective compound bacteria or batch biofilm reactor import; The highly effective compound bacteria or the batch biofilm reactor delivery port connect the advanced treating module inlet; The highly effective compound bacteria or the batch biofilm reactor sludge outlet connect the Treatment of Sludge module and enter Mouthful;
The Treatment of Sludge module includes that the sludge being sequentially connected reclaims storage pool, concentration basin and plate compression pond, the sheet frame Press filtration pond delivery port the connection highly effective compound bacteria or the batch biofilm reactor import;
The advanced treating module is divided into two parts, and a part includes ozone and activated carbon adsorption tank, and another part includes connecting successively The ultrafiltration membrance filter pond and counter-infiltration pond for connecing.
2. a kind of petrochemical industry wastewater treatment integrated technique system according to claim 1, it is characterised in that described Pretreatment module is additionally provided with acid-base accommodation system, and the acid-base accommodation system connects the water quality adjustment pond.
3. a kind of petrochemical industry wastewater treatment integrated technique system according to claim 2, it is characterised in that described Pretreatment module is additionally provided with washed-out sand pond, and washed-out sand pond sand inlet connects the rotational flow grit chamber, and delivery port connects the water quality Regulating reservoir.
4. a kind of petrochemical industry wastewater treatment integrated technique system according to claim 1, it is characterised in that described Oil removing module is additionally provided with organic polymer coargulator dosing system, and the organic polymer coargulator dosing system connects the rotation Stream flotation tank.
5. a kind of petrochemical industry wastewater treatment integrated technique system according to claim 1, it is characterised in that described Hydrolization and acidification tank or the Fenton oxidation tank and the highly effective compound bacteria or the batch biofilm reactor Connecting line is provided with three-way control valve.
6. a kind of petrochemical industry wastewater treatment integrated technique system according to claim 1, it is characterised in that described Biochemical module is additionally provided with bioengineering microbial inoculum dosing system, and the bioengineering microbial inoculum dosing system connects the high-efficiency aerobic life Thing reactor.
7. a kind of petrochemical industry wastewater treatment integrated technology process, is that, using the system described in claim 1, its feature exists In comprising the following steps:
Step one, the petroleum substance concentration of on-line monitoring analysis petrochemical industry waste water, when petroleum substance concentration≤50 Enter step 2 during mg/L, otherwise into step 3;
Petrochemical industry waste water is introduced rotational flow grit chamber desilting, after monitoring desilting by step 2, startup optimization pretreatment module PH value of waste water, and waste water after desilting is introduced into water quality adjustment pond, as pH > 8.5 or pH < 6.5, acid is added in water quality adjustment pond Or alkali is adjusted to 6.5≤pH≤8.5, is otherwise directly entered step 4;
Petrochemical industry waste water introducing oil interceptor is carried out first water-oil separating by step 3, startup optimization oil removing module, is monitored After first water-oil separating in waste water particle diameter in 0.1 ~ 10 μm of mass percent of oil particulates, when particle diameter is in 0.1 ~ 10 μm of oils During the mass percent > 50% of grain, the waste water of first water-oil separating carries out secondary water-oil separating into cyclone air-flotation pond;Work as particle diameter The dissolving oil quality of 0.1 μm of particle diameter < in 0.1 ~ 10 μm of mass percent≤50% of oil particulates and in the oil particulates During percentage > 30%, the waste water of first water-oil separating carries out secondary water-oil separating into electric flocculation system, otherwise first profit point From waste water carry out secondary water-oil separating into high strength fibre filtering ponds;Body refuse after all secondary water-oil separatings enters step Six, the waste water after all secondary water-oil separatings enters step 4;
Step 4, startup optimization biochemical module, waste water BOD at monitoring biochemical module import5/ COD value, by BOD5/ COD <'s 0.1 Waste water introduces the treatment of Fenton oxidation tank, otherwise introduces hydrolization and acidification tank treatment, monitoring Fenton oxidation tank or hydrolization and acidification tank outlet Locate the TN concentration of waste water;
Step 5, batch biofilm reactor is introduced by the waste water of TN concentration > 50mg/L, otherwise introduces high-efficiency aerobic biological Reactor;Enter step 6 from batch biofilm reactor or highly effective compound bacteria sludge out, from batch (-type) Biofilm reactor or highly effective compound bacteria waste water out enter step 7;
Step 6, starts Treatment of Sludge module, sludge is introduced sludge recovery storage pool, concentration basin and plate compression pond successively and is entered The innoxious dewater treatment of row, the mud cake outward transport after dehydration, five ~ step 6 of repeat step after sludge condensation liquid monitoring TN concentration;
Step 7, starts advanced treating module, the colourity of waste water at monitoring advanced treating module inlet, by colourity > 200 and SS The waste water of concentration > 50mg/L introduces ultrafiltration membrance filter pond and the treatment of counter-infiltration pond successively, otherwise introduces ozone and activated carbon adsorption tank Treatment.
8. a kind of petrochemical industry wastewater treatment integrated technology process according to claim 7, it is characterised in that described Step 2 by waste water introduce rotational flow grit chamber desilting, also including by after separation desilting cleaning, rinse water introduce water quality adjustment Pond carries out subsequent treatment.
9. a kind of petrochemical industry wastewater treatment integrated technology process according to claim 7, it is characterised in that described The operational factor of the hydrolization and acidification tank of step 4 is:22 ~ 25 DEG C of reaction temperature, 5 ~ 6h of hydraulic detention time, sludge retention time 2.5 ~ 3d, COD 10 ~ 16kg/ of volumetric loading (m3﹒ d).
10. a kind of petrochemical industry wastewater treatment integrated technology process according to claim 7, it is characterised in that described The operational factor of the ozone and activated carbon adsorption tank of step 7 is:Logical ozonation time 3 ~ 5min, ozone 120 ~ 140mg/L of oxygen-supply quantity, 10 ~ 15min of charcoal absorption time, charcoal post 2 ~ 2.5m of diameter, layer of charcoal height 2.5 ~ 3.0m, total residence time 25 ~ 30min are smelly The flow-rate ratio of oxygen and the waste water from biochemical treatment module out(3.5~4.0):1.
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