CN111646595A - Oil field extraction water treatment simulation experiment device - Google Patents

Oil field extraction water treatment simulation experiment device Download PDF

Info

Publication number
CN111646595A
CN111646595A CN202010539405.8A CN202010539405A CN111646595A CN 111646595 A CN111646595 A CN 111646595A CN 202010539405 A CN202010539405 A CN 202010539405A CN 111646595 A CN111646595 A CN 111646595A
Authority
CN
China
Prior art keywords
water
filter
oil
tank
pressure
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN202010539405.8A
Other languages
Chinese (zh)
Other versions
CN111646595B (en
Inventor
任永良
张国鹏
何树威
祝洪伟
程晓飞
高胜
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Northeast Petroleum University
Original Assignee
Northeast Petroleum University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Northeast Petroleum University filed Critical Northeast Petroleum University
Priority to CN202010539405.8A priority Critical patent/CN111646595B/en
Publication of CN111646595A publication Critical patent/CN111646595A/en
Application granted granted Critical
Publication of CN111646595B publication Critical patent/CN111646595B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05BCONTROL OR REGULATING SYSTEMS IN GENERAL; FUNCTIONAL ELEMENTS OF SUCH SYSTEMS; MONITORING OR TESTING ARRANGEMENTS FOR SUCH SYSTEMS OR ELEMENTS
    • G05B19/00Program-control systems
    • G05B19/02Program-control systems electric
    • G05B19/418Total factory control, i.e. centrally controlling a plurality of machines, e.g. direct or distributed numerical control [DNC], flexible manufacturing systems [FMS], integrated manufacturing systems [IMS] or computer integrated manufacturing [CIM]
    • G05B19/41865Total factory control, i.e. centrally controlling a plurality of machines, e.g. direct or distributed numerical control [DNC], flexible manufacturing systems [FMS], integrated manufacturing systems [IMS] or computer integrated manufacturing [CIM] characterised by job scheduling, process planning, material flow
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/008Control or steering systems not provided for elsewhere in subclass C02F
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/24Treatment of water, waste water, or sewage by flotation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F2001/007Processes including a sedimentation step
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/10Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus
    • C02F2201/005Valves
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/03Pressure
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/40Liquid flow rate
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/14Maintenance of water treatment installations
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P90/00Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
    • Y02P90/02Total factory control, e.g. smart factories, flexible manufacturing systems [FMS] or integrated manufacturing systems [IMS]

Landscapes

  • Engineering & Computer Science (AREA)
  • General Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Quality & Reliability (AREA)
  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Automation & Control Theory (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

本发明涉及的是一种油田采出水处理模拟实验装置,这种油田采出水处理模拟实验装置包括原水配制装置、自然沉降装置、混凝沉降装置、升压缓冲装置、过滤反冲洗装置、配药装置、污油回收装置、污泥污水处理装置、遥控位移装置、报警装置、控制台,通过自然沉降装置来模拟实际的自然沉降效果,通过加药环节,实现二次混凝沉降的效果,调整打入量的参数来实时进行控制药剂添加的多少,进而实现更加精准的控制;升压缓冲装置使上游流过来的压力和流速不稳定的混合液稳定在一个范围内,过滤反冲洗装置对含油污水进一步的分离。本发明通过对油田采出含油污水处理系统进行模拟,调节进水流量、压力以及沉降时间,达到回注水或外排水的水质标准。

Figure 202010539405

The invention relates to an oil field produced water treatment simulation experimental device. The oil field produced water treatment simulation experimental device includes a raw water preparation device, a natural sedimentation device, a coagulation sedimentation device, a pressure boosting buffer device, a filtration backwash device, and a medicine dispensing device. , sewage oil recovery device, sludge sewage treatment device, remote control displacement device, alarm device, console, simulate the actual natural settlement effect through the natural settling device, and achieve the effect of secondary coagulation and settling through the dosing process. The input parameters are used to control the amount of chemicals added in real time, so as to achieve more precise control; the pressure boosting buffer device stabilizes the mixed liquid with unstable pressure and flow rate flowing from the upstream within a range, and the filter backwash device is effective for oily sewage. further separation. The present invention achieves the water quality standard of reinjection water or external drainage by simulating the oily sewage treatment system produced in the oil field, and adjusting the flow rate, pressure and settling time of the influent water.

Figure 202010539405

Description

一种油田采出水处理模拟实验装置A simulation experiment device for oil field produced water treatment

技术领域technical field

本发明涉及的是研究油田采出水处理的实验装置,具体涉及一种油田采出水处理模拟实验装置。The invention relates to an experimental device for researching oilfield produced water treatment, in particular to a simulation experimental device for oilfield produced water treatment.

背景技术Background technique

采用注水开采的油田,从注水井注入油层的水,其中大部分通过采油井随原油一起回到地面,这部分水在原油外运和外输前必须加以脱除,脱出的污水中含有原油,因此被称为油田采出水。随着油田开采年代的增长,采水液的含水率不断上升,有的区块已达到90%以上,这些含油污水已成为油田的主要注水水源。随着油田外围低渗透油田和表外储层的连续开发,对油田注水水质的要求更加严格。油田污水主要包括原油脱出水(又名油田采出水)、钻井污水及站内其它类型的含油污水。油田污水的处理依据油田生产、环境等因素可以有多种方式。当油田需要注水时,油田污水经处理后回注地层,此时要对水中的悬浮物、油等多项指标进行严格控制,防止其对地层产生伤害。国内油田每天注水量非常大,那么相应需要处理的含油污水也非常大,耗能也非常严重,为了节省能源和更加有效地管控污水处理的工艺过程需要对油田污水处理系统进行仿真优化,通过采样分析来进行每个环节的调度,但实际的油田污水处理系统比较大,结构复杂,每个环节的调控也较难,因此利用实际的污水处理工艺设备进行实验非常困难。另一方面,对含油污水处理系统进行优化分析是势在必行,所以建立一套油田采出水处理模拟实验装置,通过对模拟污水处理实验装置进行优化设计和改进,进而来分析实际污水处理系统是一种可行的方法。In oilfields exploited by water injection, most of the water injected into the oil layer from the water injection wells returns to the ground together with the crude oil through the oil extraction wells. This part of the water must be removed before the crude oil is transported out. Therefore, it is called oilfield produced water. With the development of the oil field, the water content of the water production fluid has been rising, and some blocks have reached more than 90%. These oily sewage has become the main water source for water injection in the oil field. With the continuous development of low-permeability oilfields and off-surface reservoirs in the periphery of the oilfield, the requirements for the water quality of oilfield injection are more stringent. Oilfield sewage mainly includes crude oil dehydration water (also known as oilfield produced water), drilling sewage and other types of oily sewage in the station. There are many ways to treat oilfield sewage according to oilfield production, environment and other factors. When the oilfield needs water injection, the oilfield sewage is reinjected into the formation after treatment. At this time, many indicators such as suspended solids and oil in the water should be strictly controlled to prevent them from causing damage to the formation. The daily water injection in domestic oilfields is very large, so the oily sewage that needs to be treated is also very large, and the energy consumption is also very serious. In order to save energy and control the process of sewage treatment more effectively, it is necessary to simulate and optimize the oilfield sewage treatment system. Analysis to carry out the scheduling of each link, but the actual oilfield sewage treatment system is relatively large, the structure is complex, and the control of each link is difficult, so it is very difficult to use the actual sewage treatment process equipment to conduct experiments. On the other hand, it is imperative to optimize and analyze the oily sewage treatment system. Therefore, a set of oilfield produced water treatment simulation experimental device is established. By optimizing the design and improvement of the simulated sewage treatment experimental device, the actual sewage treatment system can be analyzed. is a feasible method.

发明内容SUMMARY OF THE INVENTION

本发明的目的是提供一种油田采出水处理模拟实验装置,这种油田采出水处理模拟实验装置用于解决利用实际的污水处理工艺设备进行实验,建模和制定优化方案非常困难的问题。The purpose of the present invention is to provide an oil field produced water treatment simulation experimental device, which is used to solve the problem that it is very difficult to use actual sewage treatment process equipment to conduct experiments, model modeling and formulate optimization plans.

本发明解决其技术问题所采用的技术方案是:这种油田采出水处理模拟实验装置包括原水配制装置、自然沉降装置、混凝沉降装置、升压缓冲装置、过滤反冲洗装置、配药装置、污油回收装置、污泥污水处理装置、自动清洗装置、遥控位移装置、报警装置、控制台,自然沉降装置包括自然沉降罐,自然沉降罐内设置进水配水结构、集水结构、集油结构、排水结构和污泥处理结构,进水配水结构包括进水部分、配水部分,进水部分的进水口处设置电控阀门,对进水流速和流量控制,并在电控阀门周围安装流量计和压力计;配水部分有多个配水口,每个配水口安装有电动控制阀,每个配水口处设置滤头,滤头连接自动装卸装置,自动装卸装置用于将布满污垢的滤头转移到清洗区清洗,再送回配水口处重新安装到,根据流速传感器和压力传感器传送的数据,在控制台系统界面实时对配水部分进行流量的控制;配水部分有自动变频搅拌装置,依据入水口速度、压力传感器信号的变化,改变搅拌装置的搅拌频率,使含油污水在沉降前充分混合;沉降罐底部开有污泥收集口,污泥收集口连接负压抽吸系统;自然沉降罐上方设置侧壁洗刮装置,侧壁洗刮装置连接自动升降组件,侧壁洗刮装置被自动升降组件送到自然沉降罐底部,进行洗刷;出水管线上安装节流调速电控阀;自然沉降罐下方设置气浮设备,气浮设备设置于支撑框架结构上,支撑框架结构两个侧边有滑轮,滑轮和轨道相接触,轨道安装在靠近罐壁的两侧;集油结构为集油槽,集油槽在靠近油层附近开设有一圈出油堰,出油堰是三角形形状,在出油堰内壁有一圈薄板,薄板安装在滑道上,在集油槽底部设计了一圈加热盘管,集油槽底面有坡度;自然沉降罐从上到下设置4个采样口,每个采样口设置一个采样装置,油水相接触的位置处设置一个采样口,往下较深处设置一个采样口,再向下在自然沉降罐中间部位设置一个采样口,最后在固液相间处开设置一个采样口,每个采样口出口处安装截止阀,截止阀另一端与软管连接,软管连接一个采样容器;The technical scheme adopted by the present invention to solve the technical problem is as follows: the oil field produced water treatment simulation experimental device includes a raw water preparation device, a natural sedimentation device, a coagulation sedimentation device, a pressure boosting buffer device, a filter backwash device, a medicine dispensing device, a sewage treatment device, and a sewage treatment device. Oil recovery device, sludge sewage treatment device, automatic cleaning device, remote control displacement device, alarm device, console, natural settling device includes natural settling tank, and the natural settling tank is provided with water inlet and water distribution structure, water collecting structure, oil collecting structure, Drainage structure and sludge treatment structure. The water inlet and water distribution structure includes the water inlet part and the water distribution part. An electric control valve is set at the water inlet of the water inlet part to control the flow rate and flow of the influent water, and a flow meter and a flow meter are installed around the electric control valve. Pressure gauge; the water distribution part has multiple water distribution ports, each water distribution port is equipped with an electric control valve, each water distribution port is provided with a filter head, and the filter head is connected to an automatic loading and unloading device. The automatic loading and unloading device is used to transfer the filter head covered with dirt Go to the cleaning area for cleaning, and then send it back to the water distribution port for re-installation. According to the data transmitted by the flow rate sensor and the pressure sensor, the flow rate of the water distribution part is controlled in real time on the console system interface; the water distribution part has an automatic frequency conversion stirring device. According to the speed of the water inlet The change of the signal of the pressure sensor changes the stirring frequency of the stirring device, so that the oily sewage is fully mixed before settling; the bottom of the settling tank has a sludge collection port, which is connected to the negative pressure suction system; the side of the natural settling tank is set up. Wall washing and scraping device, the side wall washing and scraping device is connected to the automatic lifting component, and the side wall washing and scraping device is sent to the bottom of the natural settling tank by the automatic lifting component for washing; throttling speed regulating electric control valve is installed on the water outlet pipeline; under the natural settling tank Air flotation equipment is installed, and the air flotation equipment is installed on the support frame structure. There are pulleys on both sides of the support frame structure. The pulleys are in contact with the rails, and the rails are installed on both sides near the tank wall; the oil collection structure is an oil collection tank, an oil collection tank There is an oil outlet weir near the oil layer. The oil outlet weir is triangular in shape. There is a circle of thin plates on the inner wall of the oil outlet weir. The thin plates are installed on the slideway. A heating coil is designed at the bottom of the oil collecting tank. ; The natural sedimentation tank is provided with 4 sampling ports from top to bottom, each sampling port is equipped with a sampling device, a sampling port is set at the position where the oil and water are in contact, a sampling port is set deeper down, and then the natural sedimentation is set downward. A sampling port is set in the middle of the tank, and finally a sampling port is set between the solid and liquid phases. A stop valve is installed at the outlet of each sampling port, and the other end of the stop valve is connected to a hose, and the hose is connected to a sampling container;

混凝沉降装置比自然沉降装置多一个斜板结构,斜板结构由多个塑料波纹板组合而成,塑料波纹板呈喇叭状,多个塑料波纹板由内到外一层层相间组合,相邻两个塑料波纹板之间有固定连接的结构,斜板置于支撑结构上,斜板的上部开有吊环;The coagulation settling device has one more inclined plate structure than the natural settling device. The inclined plate structure is composed of a plurality of plastic corrugated plates. The plastic corrugated plates are horn-shaped. There is a fixed connection structure between two adjacent plastic corrugated plates, the inclined plate is placed on the support structure, and the upper part of the inclined plate is provided with a lifting ring;

升压缓冲装置包括筒体、报警装置、过滤网,过滤网可拆卸地设置于升压缓冲装置底部,过滤网下面设置排污口,升压缓冲装置使上游流过来的压力和流速不稳定的混合液稳定在一个范围内,离筒体入口半米的位置处安装有压力传感器、流量传感器,筒体右端为出口,出口与出水管线相连,出水管线与出口相间处安装升压装置,出口也安装流量传感器和压力传感器;筒体紧贴过滤网的侧壁处有设置矩形的密封口,滤网的清洗与更换通过洗密封口移出筒体;根据压力传感器和流量传感器传送的数据确定混合液需要在缓冲装置的停留时间,如果压力和流量过大,则报警装置产生警报;The booster buffer device includes a cylinder body, an alarm device, and a filter screen. The filter screen is detachably arranged at the bottom of the booster buffer device. A sewage outlet is arranged under the filter screen. The booster buffer device makes the upstream pressure and flow rate unstable. The liquid is stable within a range. A pressure sensor and a flow sensor are installed at a position half a meter away from the inlet of the cylinder. The right end of the cylinder is the outlet. The outlet is connected to the water outlet pipeline. Flow sensor and pressure sensor; there is a rectangular sealing port at the side wall of the cylinder close to the filter screen, and the cleaning and replacement of the filter screen is removed from the cylinder body through the cleaning and sealing port; according to the data transmitted by the pressure sensor and the flow sensor, the mixed liquid needs are determined During the dwell time of the buffer device, if the pressure and flow are too large, the alarm device will generate an alarm;

过滤反冲洗装置包括过滤罐、进水配水装置、滤头筛网结构、滤料层、衬托层、集水机构、分层分频搅拌加压冲洗装置、污泥污垢收集结构、反冲洗回路结构、压力报警器,滤料层更换与清洗结构,滤料层有三层,集水机构是反冲洗时的配水结构,集水机构由几个带喷孔的管子组成,正常工作时,滤后水会经过集水结构排出过滤反冲洗装置,反冲洗时,反冲洗的集水机构,通过喷孔向上喷出完成反冲;分层分频搅拌加压冲洗装置,在滤料层的每一层均对应设置一个搅拌桨,每层搅拌桨的桨叶大小、个数以及倾斜角度不同,搅拌桨设置带有小孔的管径装置,在搅拌桨旋转的同时,洁净的清水以一定的压力通过小孔然后喷射到滤料中去,使得滤料得到进一步的清洗;污泥污垢收集结构设置在过滤罐底部,过滤罐底部为椭球形状,底部具有凹坑,凹坑底部安装根据压力进行自动开合的阀门机构,洗刷头靠近椭球面设置,洗刷头依据设定好的螺旋轨道进行对椭球面清刮,到达底部后,洗刷头上的污垢基于重力的作用掉入凹坑,等到沉积物重量达到设定的压力值之后,阀门机构自行打开。The filter backwash device includes a filter tank, an inlet water distribution device, a filter head screen structure, a filter material layer, a backing layer, a water collection mechanism, a layered frequency division stirring and pressure washing device, a sludge and dirt collection structure, and a backwash circuit structure. , pressure alarm, filter material layer replacement and cleaning structure, the filter material layer has three layers, the water collecting mechanism is the water distribution structure during backwashing, and the water collecting mechanism is composed of several pipes with nozzle holes. It will be discharged from the filter backwashing device through the water collecting structure. During backwashing, the backwashing water collecting mechanism will spray upward through the nozzle hole to complete the backwashing; the layered frequency division stirring and pressure washing device is used in each layer of the filter material layer. There is a corresponding stirring paddle. The size, number and inclination angle of each layer of stirring paddle are different. The stirring paddle is equipped with a pipe diameter device with small holes. When the stirring paddle rotates, clean water passes through at a certain pressure. The small holes are then sprayed into the filter material, so that the filter material can be further cleaned; the sludge and dirt collection structure is set at the bottom of the filter tank, the bottom of the filter tank is in the shape of an ellipsoid, and the bottom has a pit, and the bottom of the pit is installed automatically according to the pressure. The opening and closing valve mechanism, the scrub head is set close to the ellipsoid surface, and the scrub head scrapes the ellipsoid surface according to the set spiral track. After reaching the bottom, the dirt on the scrub head falls into the pit based on the action of gravity, and waits until the sediment After the weight reaches the set pressure value, the valve mechanism opens on its own.

上述方案中控制台通过网络连接手机APP,实现进一步地自动化,能够在远程就能监控整个系统的运作,用户可以通过这个手机客户端方便地了解到整个系统的运行情况,而且在这个APP中还提供警报系统,当整个系统装置出现异常情况时,系统会将异常状况上传到手机客户端,及时的提醒客户有紧急状况需要处理。In the above scheme, the console is connected to the mobile APP through the network to achieve further automation, and the operation of the entire system can be monitored remotely. Users can easily understand the operation of the entire system through the mobile client. Provide an alarm system. When the whole system device has an abnormal situation, the system will upload the abnormal situation to the mobile phone client, and promptly remind the customer that there is an emergency situation that needs to be dealt with.

上述方案中配药装置通过隔板设置多个放置药物的空闲区,每个空闲区均为长方体的形状,每个空闲区的两端都开有孔,一端安装自动调节阀门,另一端与带有泵机的管路相连接,自动调节阀门与控制电路相连,控制台通过相应的自动调节阀门,控制某种药剂的添加;每个隔板的上下位置都安置有液位传感器,用来对液位的监测,当液位高于最高位或者低于最低位时,液位传感器会把信号给报警系统,通知控制台采取应急措施,当液位过高时,关闭自动调节阀门,停止对药库的补加,当液位显示过低时,会加大泵机的回转速度,及时往药库添加所需要的药剂。In the above scheme, the dispensing device is provided with a plurality of free areas for placing medicines through the partition, each free area is in the shape of a cuboid, and both ends of each free area are provided with holes, one end is installed with an automatic adjustment valve, and the other end is connected with a The pipeline of the pump is connected, the automatic adjustment valve is connected with the control circuit, and the console controls the addition of a certain drug through the corresponding automatic adjustment valve; the upper and lower positions of each partition are equipped with liquid level sensors, which are used to adjust the liquid level. Level monitoring, when the liquid level is higher than the highest level or lower than the lowest level, the liquid level sensor will send a signal to the alarm system, informing the console to take emergency measures, when the liquid level is too high, close the automatic adjustment valve and stop the medicine For the replenishment of the warehouse, when the liquid level is displayed too low, the rotation speed of the pump will be increased, and the required medicine will be added to the medicine warehouse in time.

上述方案中污泥污水处理装置采用敞口的长方体大铁箱,底部设计成漏斗的形状,中间用隔板分开形成污泥池和污水池,锥形底部与管线相连接,锥形底部与管线通过法兰与带有压力传感器的阀门相连接。In the above scheme, the sludge sewage treatment device adopts an open cuboid iron box, the bottom is designed in the shape of a funnel, the sludge tank and the sewage tank are separated by a partition in the middle, the conical bottom is connected with the pipeline, and the conical bottom is connected with the pipeline. The valve is connected to a valve with a pressure sensor by means of a flange.

上述方案中污油回收装置为污油回收罐,罐体分为三层,每层都有一个网格大小不同的滤网,使得污油在往下沉降的过程中筛掉一部分杂质,出油口处也包含一个滤网,每个滤网附近处安装一个压力传感器和一个报警装置,当某一部分滤网上的杂质过多导致此处的压力升高时,报警装置进行提醒更换和清洗该处滤网;罐体内壁设置从顶到底的螺旋加热管线,顶部为进热水口,底部为出热水口,由于环境的变化,有时罐中的油流动缓慢,不能满足设备的处理要求,此时通过提高油的温度,可以减小污油的粘度进而提高油的流动性。污油回收装置长时间的使用会积累大量的油污,装置内的加热管线以及滤网通过吊环可以起吊到外部进行清洗和更换。In the above scheme, the sewage oil recovery device is a sewage oil recovery tank. The tank body is divided into three layers, and each layer has a filter screen with different mesh sizes, so that the sewage oil can screen out some impurities in the process of sedimentation, and the oil can be discharged. There is also a filter screen at the mouth. A pressure sensor and an alarm device are installed near each filter screen. When too much impurities on a certain part of the filter screen cause the pressure here to rise, the alarm device will remind you to replace and clean the place. Filter screen; the inner wall of the tank is provided with a spiral heating pipeline from the top to the bottom. The top is the hot water inlet and the bottom is the hot water outlet. Due to changes in the environment, sometimes the oil in the tank flows slowly and cannot meet the processing requirements of the equipment. By increasing the temperature of the oil, the viscosity of the dirty oil can be reduced and the fluidity of the oil can be improved. The long-term use of the sewage oil recovery device will accumulate a large amount of oil pollution. The heating pipeline and the filter screen in the device can be lifted to the outside through the lifting ring for cleaning and replacement.

上述方案中侧壁洗刮装置利用自动变频搅拌装置的转动轴,转动轴通过分离机构、传动机构连接侧壁洗刮装置,利用分离机构,当进行清洗时,转动轴通过传动机构和侧壁洗刮装置进行连接,洗刷强度通过变频泵来进行调节,通过控制台的信号控制对变频泵的速度大小进行调节,从而使得洗刷过程更为灵活,为了使罐壁洗的更为彻底,在转运轴设置上下升降的移动装置。In the above scheme, the side wall washing and scraping device uses the rotating shaft of the automatic frequency conversion stirring device, and the rotating shaft is connected to the side wall washing and scraping device through the separation mechanism and the transmission mechanism. The scraping device is connected, the scrubbing intensity is adjusted by the frequency conversion pump, and the speed of the frequency conversion pump is adjusted through the signal control of the console, so that the scrubbing process is more flexible. Set up and down the mobile device.

上述方案中污泥污垢收集结构包括洗刷头和螺旋轨道,洗刷头可伸缩、可自转,螺旋轨道截面为矩形,洗刷头包括毛刷、洗刷头盒,洗刷头盒内部设置正反转可控的小型电动机和洗刷控制器,洗刷头盒侧边设置两个行走轮,洗刷头盒设置轨道孔,螺旋轨道从轨道孔穿过,洗刷头盒与螺旋轨道滑动连接,螺旋轨道的起始端和末端设置位置传感器。In the above scheme, the sludge and dirt collection structure includes a scrubbing head and a spiral track. The scrubbing head is retractable and self-rotating. The cross section of the spiral track is rectangular. The scrubbing head includes a brush and a scrubbing head box. Small motor and scrub controller, two walking wheels are arranged on the side of the scrub head box, the scrub head box is provided with a track hole, the spiral track passes through the track hole, the scrub head box is slidably connected with the spiral track, and the start and end of the spiral track are set position sensor.

上述方案中进水配水装置的配水管围绕中轴进行缓慢匀速的旋转,这样可以使得配水更为均匀。In the above solution, the water distribution pipe of the water inlet and water distribution device rotates slowly and uniformly around the central axis, which can make the water distribution more uniform.

上述方案中过滤反冲洗装置的滤料层分为三部分,从上往下粒径越来越大,最上层滤料为粒径细的细沙,中间滤料是粒径较细的粗砂,最下面滤料为粒径较大的砾石,砾石下方衬托层,衬托层支撑滤料层。In the above scheme, the filter material layer of the filter backwash device is divided into three parts, the particle size is getting larger and larger from top to bottom, the top filter material is fine sand with fine particle size, and the middle filter material is coarse sand with fine particle size , the bottom filter material is gravel with larger particle size, and the backing layer under the gravel supports the filter material layer.

上述方案中分层分频搅拌加压冲洗装置在三层搅拌桨,最上层搅拌桨有8个桨叶,中间第二层搅拌桨有6个桨叶,第三层搅拌桨有4个桨叶。In the above scheme, the layered and frequency-distributed stirring and pressurized flushing device is located in a three-layer stirring paddle, the top-layer stirring paddle has 8 paddles, the middle second-layer stirring paddle has 6 paddles, and the third-layer stirring paddle has 4 paddles .

本发明具有以下有益效果:The present invention has the following beneficial effects:

1、本发明能够模拟不同成分不同温度的含油污水,不同速度不同压力条件下的流体情况,以及不同条件下自然沉降所需时间长短和速度大小,过滤时压强大小的选择以及药物选择和加药多少的配比等,通过调节水泵频率大小和压力调节装置的强度,从而改变水流速度和压强大小,通过控制台改变相应位置处阀门的开度,进而来改变流量的大小等措施来进行测试,以得出实验数据,获得最佳流速、压力、时间、药物配比、加药强度以及其它一些参数,从而达到最佳污水处理效果以及最大化的节省能源。1. The present invention can simulate oily sewage with different components and different temperatures, fluid conditions at different speeds and pressures, as well as the length of time and speed required for natural sedimentation under different conditions, and the selection of pressure during filtration, as well as drug selection and dosing. How many proportions, etc., by adjusting the frequency of the pump and the strength of the pressure regulating device, thereby changing the speed of the water flow and the pressure, and changing the opening of the valve at the corresponding position through the console to change the flow rate and other measures to test, In order to obtain experimental data, obtain the best flow rate, pressure, time, drug ratio, dosing strength and other parameters, so as to achieve the best sewage treatment effect and maximize energy saving.

2、实际油田污水处理系统结构复杂,占地面积大,对于整个系统的控制和检测都存在较大的困难,因此利用实际的污水处理工艺设备进行实验,建模和制定优化方案非常困难。迄今为止,国内外尚未见到现成的理论方法,且不能用经典数学和优化方法解决。本发明是一种新型的,能够实现自动化和云服务的模拟装置。它适用于实验室内观察、采样分析、数据采集和对系统的优化分析,通过对模拟污水处理实验装置进行优化设计和改进,进而来分析实际污水处理系统是一种可行的方法。2. The actual oilfield sewage treatment system has a complex structure and a large area, and it is difficult to control and detect the entire system. Therefore, it is very difficult to use the actual sewage treatment process equipment to conduct experiments, model modeling and formulate optimization plans. So far, there is no ready-made theoretical method at home and abroad, and it cannot be solved by classical mathematics and optimization methods. The present invention is a novel simulation device capable of realizing automation and cloud service. It is suitable for observation, sampling analysis, data acquisition and optimization analysis of the system in the laboratory. It is a feasible method to analyze the actual sewage treatment system by optimizing the design and improvement of the simulated sewage treatment experimental device.

3、本发明考虑到了实际油田采出水处理时沉降环节、升压缓冲环节、过滤反冲洗环节等各个环节流体的速度、压力以及各设备液体停留时间等参数难以控制的问题。通过在每个环节的进水口和出水口处设置有流量、压力传感器,通过这些传感器收集的数据可以很方便地进行相应位置的管控,系统中采用的是电动控制阀,一般传感器设置的有所需的范围参数,一旦数据有异常,电动控制阀会收到来自控制台的控制信号进而进行接下来的操作。3. The present invention takes into account the problems that parameters such as the velocity and pressure of the fluid in each link, such as the sedimentation link, the pressure boosting buffer link, and the filtering and backwashing link, as well as the liquid residence time of each equipment, are difficult to control in the actual oilfield produced water treatment. By setting the flow and pressure sensors at the water inlet and outlet of each link, the data collected by these sensors can easily control the corresponding position. The system uses an electric control valve. Generally, the sensor settings are somewhat different. The required range parameters, once the data is abnormal, the electric control valve will receive the control signal from the console to carry out the next operation.

4、沉降和过滤是核心部件,本发明设计了自动变频搅拌装置和分层搅拌装置,通过搅拌装置针对不同情况下的液体进行相应速度、力度的大小调节,使得含油液体能够以最合理的结构进行充分均匀的沉降凝结。4. Sedimentation and filtration are the core components. The present invention designs an automatic frequency conversion stirring device and a layered stirring device. Through the stirring device, the corresponding speed and strength are adjusted according to the liquid under different conditions, so that the oil-containing liquid can have the most reasonable structure. Sufficient and uniform settling coagulation is carried out.

5、本发明实现了自动控制和远程监控的功能,基于设备整体体积较小,采用无线传输系统,基于局域网技术,将每个需要控制的环节的参数上传到控制台和手机APP,当工作人员不在现场时,通过手机客户端也能实时地进行对整个系统的监控。5. The present invention realizes the functions of automatic control and remote monitoring. Based on the small overall size of the equipment, the wireless transmission system is adopted. Based on the local area network technology, the parameters of each link that needs to be controlled are uploaded to the console and the mobile phone APP. When not on site, the entire system can also be monitored in real time through the mobile phone client.

附图说明Description of drawings

图1a是本发明的总装图。Figure 1a is a general assembly drawing of the present invention.

图1b是本发明的立体图。Figure 1b is a perspective view of the present invention.

图2a是本发明自然沉降装置内部结构总装图。Figure 2a is a general assembly drawing of the internal structure of the natural settling device of the present invention.

图2b是本发明自然沉降装置内部结构总装图的立体图。Figure 2b is a perspective view of the general assembly drawing of the internal structure of the natural settling device of the present invention.

图3是本发明进水部分中进水管的结构示意图。FIG. 3 is a schematic structural diagram of the water inlet pipe in the water inlet part of the present invention.

图4是本发明进水部分中心集水管的结构示意图。4 is a schematic structural diagram of the central water collecting pipe of the water inlet part of the present invention.

图5是本发明配水部分中配水管的结构示意图。Figure 5 is a schematic structural diagram of the water distribution pipe in the water distribution part of the present invention.

图6是本发明出水部分中出水管的结构示意图。FIG. 6 is a schematic structural diagram of the water outlet pipe in the water outlet part of the present invention.

图7是本发明集油槽结构示意图。Figure 7 is a schematic diagram of the structure of the oil collecting tank of the present invention.

图8是本发明集油槽底部加热盘管结构示意图。FIG. 8 is a schematic structural diagram of the heating coil at the bottom of the oil collecting tank of the present invention.

图9是本发明采样装置结构示意图。FIG. 9 is a schematic structural diagram of the sampling device of the present invention.

图10是本发明混凝沉降装置中的斜板结构示意图。Fig. 10 is a schematic diagram of the inclined plate structure in the coagulation and settling device of the present invention.

图11是本发明混凝沉降装置中支撑结构示意图。Figure 11 is a schematic diagram of the support structure in the coagulation and settling device of the present invention.

图12是本发明侧壁刮洗装置结构示意图。12 is a schematic structural diagram of the sidewall scraping device of the present invention.

图13是本发明污泥污水收集结构示意图。Figure 13 is a schematic diagram of the sludge sewage collection structure of the present invention.

图14是本发明污泥污水收集结构中洗刷头结构示意图。Figure 14 is a schematic diagram of the structure of the scrub head in the sludge sewage collection structure of the present invention.

图15是本发明洗刷头的螺旋轨道图。Figure 15 is a spiral trajectory diagram of the scrub head of the present invention.

图16是本发明自动变频搅拌装置的结构示意图。16 is a schematic structural diagram of the automatic frequency conversion stirring device of the present invention.

图17是本发明遥控位移装置的滚轮结构示意图。FIG. 17 is a schematic view of the roller structure of the remote control displacement device of the present invention.

图18是本发明可以自动升降的起吊装置结构示意图。FIG. 18 is a schematic structural diagram of the hoisting device that can automatically go up and down according to the present invention.

图19是本发明气浮装置结构示意图。Figure 19 is a schematic view of the structure of the air flotation device of the present invention.

图20是本发明气浮装置安装固定结构示意图。Figure 20 is a schematic diagram of the installation and fixing structure of the air flotation device of the present invention.

图21是本发明支撑框架结构中滑轮轨道结构示意图。Figure 21 is a schematic diagram of the pulley track structure in the support frame structure of the present invention.

图22是本发明用来起吊设备的升降装置结构示意图。Figure 22 is a schematic structural diagram of a lifting device used for lifting equipment according to the present invention.

图23是本发明中升压缓冲装置结构示意图。FIG. 23 is a schematic structural diagram of the boosting buffer device in the present invention.

图24是本发明中过滤反冲洗装置结构示意图。Figure 24 is a schematic structural diagram of the filter backwashing device in the present invention.

图25是本发明过滤反冲洗装置配水系统中的筛管结构示意图。Figure 25 is a schematic diagram of the structure of the screen in the water distribution system of the filter backwash device of the present invention.

图26是本发明所述的过滤反冲洗装置中滤头转换结构示意图。Figure 26 is a schematic diagram of the filter head switching structure in the filter backwashing device according to the present invention.

图27是本发明所述的过滤反冲洗装置中分层分频搅拌加压冲洗装置结构示意图。27 is a schematic structural diagram of a layered and frequency-distributed stirring and pressure washing device in the filter backwashing device according to the present invention.

图28是本发明所述的过滤反冲洗装置中的滤网结构示意图。Figure 28 is a schematic diagram of the structure of the filter screen in the filter backwashing device according to the present invention.

图29是本发明所述的过滤反冲洗装置中的反冲洗进水配水结构示意图。FIG. 29 is a schematic diagram of the structure of backwashing influent water distribution in the filter backwashing device according to the present invention.

图30是本发明所述的过滤反冲洗装置中位于底部的支撑结构示意图。Figure 30 is a schematic diagram of the support structure at the bottom of the filter backwashing device according to the present invention.

图31是本发明所述的过滤反冲洗装置中支撑装置的铰接结构示意图。Figure 31 is a schematic diagram of the hinged structure of the support device in the filter backwashing device according to the present invention.

图32是本发明所述支撑框架结构中工字钢结构示意图。Figure 32 is a schematic diagram of the I-beam structure in the support frame structure of the present invention.

图33是本发明中配药装置结构示意图。Figure 33 is a schematic diagram of the structure of the dispensing device in the present invention.

图34是本发明中污油回收装置结构示意图。FIG. 34 is a schematic structural diagram of the dirty oil recovery device in the present invention.

图35是本发明所述的污油回收装置中的空间螺旋加热盘管结构示意图。FIG. 35 is a schematic structural diagram of the space spiral heating coil in the sewage oil recovery device according to the present invention.

图36是本发明所述的污泥污水处理装置结构示意图。Figure 36 is a schematic structural diagram of the sludge sewage treatment device according to the present invention.

图37是本发明控制台结构示意图。Figure 37 is a schematic diagram of the structure of the console of the present invention.

图中:1自然沉降装置,2.混凝沉降装置,3进水管,4中心集水管,5配水管,6出水管,7集油槽,8加热盘管,9采样装置,10斜板结构,11支撑结构,12侧壁刮洗装置,13洗刷头盒,14洗刷头,15螺旋轨道,16自动变频搅拌装置,17滚轮,18起吊装置,19气浮装置,20气浮装置安装固定结构,21滑轮,22升降装置,23升压缓冲装置,24过滤反冲洗装置,25滤头筛网结构,26滤头转换结构,27分层分频搅拌加压冲洗装置,28滤网,29集水机构,30衬托层,33配药装置,34污油回收装置,35螺旋加热管线,36污泥污水处理装置,37控制台,38行走轮,39位置传感器,40轨道孔。In the figure: 1. Natural settling device, 2. Coagulation settling device, 3. Water inlet pipe, 4. Central water collecting pipe, 5. Water distribution pipe, 6. Water outlet pipe, 7. Oil collecting tank, 8. Heating coil, 9. Sampling device, 10. Inclined plate structure, 11 Supporting structure, 12 Side wall scraping device, 13 Washing head box, 14 Washing head, 15 Spiral track, 16 Automatic frequency conversion stirring device, 17 Roller, 18 Lifting device, 19 Air flotation device, 20 Installation and fixing structure of air flotation device, 21 pulley, 22 lift device, 23 boost buffer device, 24 filter backwash device, 25 filter head screen structure, 26 filter head conversion structure, 27 layered frequency division stirring pressure washing device, 28 filter screen, 29 water collection Mechanism, 30 lining layer, 33 dispensing device, 34 sewage oil recovery device, 35 spiral heating pipeline, 36 sludge sewage treatment device, 37 console, 38 traveling wheel, 39 position sensor, 40 track hole.

具体实施方式Detailed ways

下面结合附图对本发明作进一步的说明:Below in conjunction with accompanying drawing, the present invention is further described:

结合图1-图37所示,这种油田采出水处理模拟实验装置包括原水配制装置、自然沉降装置1、混凝沉降装置2、升压缓冲装置23、过滤反冲洗装置24、配药装置33、污油回收装置34、污泥污水处理装置36、自动清洗装置、遥控位移装置、报警装置、控制台37。本发明是通过对油田采出含油污水处理系统进行模拟,调节进水流量、压力以及沉降时间,以达到回注水或外排水的水质标准。两级沉降装置(自然沉降装置1、混凝沉降装置2)进行沉降包括模拟实际污水处理时的物理沉降分离,污油的收集以及加药处理后的混凝沉降,用于测量和显示水流方向的流向测量装置,用于测量水流流速和压力的传感器。一次沉降罐也称为物理沉降环节,用于模拟实际含油污水处理时的自然沉降,自然沉降装置1(一次沉降装置)包括进水管3、配水系统、集水系统、中心集水管4、中心集水筒、出水管6、集油装置和污泥排出结构,气浮系统,自动清洗罐壁以及罐底系统,还包括移动和固定结构。混凝沉降装置2(二次沉降装置)和自然沉降装置1类似,也包含有进水管3、配水系统、集水系统、中心集水管4、中心集水筒、出水管6、集油装置和污泥处理结构,另外还有斜板结构10,增加污水沉降的效果,此外,为了使药量能比较精确地加入到此装置中,在相应的管线中设置的有电动控制阀和带有显示屏的流量计,通过查看流量表的变化,改变对应的电动阀门大小进而来控制药量的多少。升压缓冲装置23主要是使从上一环节流过来的水流可能压力比较不稳定,那么经过缓冲装置的处理后,水流处于一个较为稳定的状态,接着再进行进一步的升压过程后流入到下一环节。过滤环节是对含油污水进一步的分离,主要包含配水系统、滤料层、排水系统以及反冲洗的结构设计。With reference to Figures 1 to 37, the simulated experimental device for the treatment of produced water in the oil field includes a raw water preparation device, a natural sedimentation device 1, a coagulation sedimentation device 2, a pressure boosting buffer device 23, a filtration backwash device 24, a dispensing device 33, Slop oil recovery device 34 , sludge sewage treatment device 36 , automatic cleaning device, remote displacement device, alarm device, console 37 . The invention adjusts the flow rate, pressure and settling time of the influent water by simulating the oily sewage treatment system produced in the oil field, so as to achieve the water quality standard of the reinjection water or the external drainage. The two-stage settling device (natural settling device 1, coagulation settling device 2) performs settling, including physical settling and separation simulating actual sewage treatment, collection of sewage oil, and coagulation settling after chemical treatment, which is used to measure and display the direction of water flow The flow direction measuring device is a sensor for measuring the flow rate and pressure of water flow. The primary settling tank is also called the physical settling link, which is used to simulate the natural settling during the actual treatment of oily sewage. Water tank, water outlet pipe 6, oil collecting device and sludge discharge structure, air flotation system, automatic cleaning tank wall and tank bottom system, also including mobile and fixed structures. The coagulation settling device 2 (secondary settling device) is similar to the natural settling device 1, and also includes a water inlet pipe 3, a water distribution system, a water collection system, a central water collection pipe 4, a central water collection cylinder, a water outlet pipe 6, an oil collection device and sewage. The mud treatment structure and the inclined plate structure 10 increase the effect of sewage sedimentation. In addition, in order to make the amount of medicine added to the device more accurately, there are electric control valves and display screens in the corresponding pipelines. The flowmeter can control the amount of medicine by checking the change of the flowmeter and changing the size of the corresponding electric valve. The pressure boosting buffer device 23 is mainly to make the pressure of the water flow from the previous link relatively unstable, so after the treatment of the buffer device, the water flow is in a relatively stable state, and then it flows into the lower pressure after further boosting process. a segment. The filtration step is to further separate the oily sewage, which mainly includes the structural design of the water distribution system, the filter material layer, the drainage system and the backwash.

原水配制装置主要为整个模拟实验系统装置提供水源,为了模拟实际的油田采出水的物理组成,用配水装置可以满足实验所需要的介质。能源动力系统为整个装置提供了水流所需要的压力,使原水能够以一定的速度在整个系统中进行输运。The raw water preparation device mainly provides water source for the whole simulation experiment system device. In order to simulate the physical composition of the actual oil field produced water, the water distribution device can meet the medium required by the experiment. The energy power system provides the pressure required by the water flow for the whole device, so that the raw water can be transported in the whole system at a certain speed.

沉降系统主要由两个部分组成,分别为自然沉降和混凝沉降。其中一次沉降装置也称之为自然沉降,含油污水通过重力的作用使得因各个物质(主要是油和水)的密度不同从而经过一定的时间后进行分离。该一次沉降装置在进水部分中设置的电控阀门,根据需要以及实验效果分析来进行对进水流速和流量的控制,电控阀门安装在进水部分的进水口处,并在其周围安装有显示屏的流量计和压力计。配水部分总共有八个出水口,每个配水口安装有电动控制阀,基于实际情况的变化可以通过控制电动控制阀的信号变化来改变每个阀口的状态,共有八个配水口,每个配水口有开和关这两种工作形式,那么总共就有十六个状态,每个配水口处都设计了一个可以自动更换的滤头,根据其每个滤头上滤网的结垢情况自行更换备用的滤头,布满污垢的滤头经过自动装卸装置被转移到清洗区,之后再被送回来重新安装到原来的位置,根据流速传感器和压力传感器回传回来的数据可以在控制台37界面及时地对配水部分进行流量的控制,当流量过大时可以控制几个配水口的阀门将其关闭,相反,当流量压力较小时就可以多开几个阀门;在配水系统下方有一个可以自动变频搅拌装置16,根据来水情况的不同,可以自动调节其搅动频率、力度和方向,而且在竖直方向也可以进行移动,这样就可以很方便地移出搅拌桨进而进行清洗。沉降罐底部开有口,用来收集污泥,用一个软管连接到此处开口,另一端接到一个类似于吸尘器功能的负压抽吸系统,此系统能够将污泥和其他污垢吸出,接着底部进一步的清洗将通过整个装置上方的侧壁洗刮装置12,经过自动升降组件,此侧壁洗刮装置达到底部然后开始洗刷,洗刷掉的污垢同样可以一同被负压抽吸系统处理掉;出水管线上安装节流调速电控阀,此阀根据下游的处理情况进行相应的调节,如果下面环节来不及处理,下游会传给此处一个报警信号,然后控制系统接收到此报警信号后会及时做出响应,暂时关闭输出阀门的开关,等待下游处理完成后,控制系统再将此处阀门打开,然后继续正常的工作。在自然沉降罐的下方安置有一排气浮装置19,气浮装置19通过气浮装置安装固定结构20安装,图20为气浮装置安装固定结构,气浮装置19根据进水量以及强度大小,气浮装置19可以调整产生气泡产生的量、大小以及频率,从而适应污水的沉降处理效果,使得液体和固体能够充分地进行分离。支撑框架结构是用来放置气浮装置19,托运气浮设备换洗的,支撑框架结构两个侧边有滑轮装置,滑轮21和轨道相接触,轨道安装在靠近罐壁的两侧,当气浮装置19需要定期清洗或维修时,支撑框架结构会依靠轨道进而拖着气浮装置19一起移动到自然沉降罐外部(自然沉降罐壁设置气浮装置开口),然后进行相应的处理。集油装置采用的是集油槽7,集油槽7由槽钢制作而成,在靠近油层附近开设的有出油堰,出油堰是三角形形状,在三角形堰的内壁有一圈薄板,薄板安装在滑道上面,根据油层的厚度可以自行调节,在集油槽7的下方设计了一圈随外界温度变化可以加热到不同温度的加热系统,加热系统采用的物理结构是一个空间的螺旋管式加热盘管8,有时油层流动比较缓慢,为了方便油层能够及时的排到集油系统,利用升高温度减小油层粘度的原理,使得油层可以更加顺利地流入到集油系统中,另外,在出油口附近的集油槽7底面设计了一个坡度,这样更有利于油的流入和流出,减少积油现象的产生。侧壁刮洗装置12,利用同一个中心转动轴,这个转动轴和自动变频搅拌装置16的转动轴是同一个转动轴,转动轴通过分离机构、传动机构连接侧壁洗刮装置,分离机构可将转动轴与传动机构连接或分开,传动机构与侧壁刮洗装置连接,利用分离机构,当需要进行清洗时,齿轮和侧壁洗刮装置进行连接,洗刷强度可以通过变频泵来进行调节,通过控制台37的信号控制可以对泵的速度大小进行调节,从而使得洗刷过程更为灵活,为了使罐壁洗的更为彻底,在中心轴的位置加了一个可以上下升降的升降装置22。采样装置9,为了能够得知实验效果,有一部分数据需要采集装置内部的混合液体,自然沉降罐根据高度的不同共设置了4个采样口,每个采样口设置一个采样装置9,油水相接触的位置处开了一个采样口,往下紧接着较深处开了一个采样口,再接着在沉降中间部位设置一个采样口,最后在固液相间处开设一个采样口,这样就可以根据不同的部位分别进行取样,然后再进行相关的实验,每个采样口出口处安装了截止阀,阀门一端与采样口连接,另一端与软管进行连接,软管与最终装采样液的容器相连接,当需要进行采样时,打开相应的阀门。The settlement system is mainly composed of two parts, namely natural settlement and coagulation settlement. The first settling device is also called natural settling. The oily sewage is separated after a certain period of time due to the different density of each substance (mainly oil and water) due to the action of gravity. The electric control valve set in the water inlet part of the primary sedimentation device controls the flow rate and flow of the influent water according to the needs and the analysis of the experimental effect. The electric control valve is installed at the water inlet of the water inlet part and is installed around it. Flow meter and pressure gauge with display. The water distribution part has a total of eight water outlets, and each water distribution port is equipped with an electric control valve. Based on the actual situation, the state of each valve port can be changed by controlling the signal change of the electric control valve. There are eight water distribution ports. The water distribution port has two working modes: open and closed, so there are sixteen states in total. Each water distribution port is designed with a filter head that can be automatically replaced, according to the scale of the filter screen on each filter head. Replace the spare filter head by yourself. The filter head covered with dirt is transferred to the cleaning area through the automatic loading and unloading device, and then sent back to the original position. 37 The interface controls the flow of the water distribution part in time. When the flow is too large, it can control the valves of several water distribution ports to close it. On the contrary, when the flow pressure is small, several more valves can be opened; The frequency conversion stirring device 16 can be automatically adjusted, and its stirring frequency, strength and direction can be automatically adjusted according to the different water conditions, and it can also be moved in the vertical direction, so that the stirring paddle can be easily removed for cleaning. There is an opening at the bottom of the sedimentation tank to collect sludge, a hose is connected to the opening, the other end is connected to a negative pressure suction system similar to the function of a vacuum cleaner, this system can suck out sludge and other dirt, Then further cleaning of the bottom will pass through the sidewall scrubbing device 12 above the entire device, and through the automatic lift assembly, the sidewall scrubbing device reaches the bottom and then starts to scrub, and the scrubbed dirt can also be processed by the negative pressure suction system. ; A throttle and speed regulating electric control valve is installed on the water outlet line, and the valve is adjusted according to the downstream processing conditions. If the following links are too late, the downstream will send an alarm signal here, and then the control system will receive the alarm signal. It will respond in time and temporarily close the switch of the output valve. After the downstream processing is completed, the control system will open the valve here, and then continue to work normally. An exhaust flotation device 19 is arranged below the natural sedimentation tank. The air flotation device 19 is installed by the air flotation device installation and fixing structure 20. Figure 20 shows the installation and fixing structure of the air flotation device. The floating device 19 can adjust the amount, size and frequency of the generated bubbles, so as to adapt to the sedimentation treatment effect of the sewage, so that the liquid and the solid can be fully separated. The support frame structure is used to place the air flotation device 19, and the flotation equipment is checked for cleaning. There are pulley devices on both sides of the support frame structure. The pulleys 21 are in contact with the rails. When the device 19 needs to be cleaned or maintained regularly, the supporting frame structure will rely on the rails and then drag the air flotation device 19 to move to the outside of the natural settling tank (the air flotation device opening is set on the wall of the natural settling tank), and then carry out corresponding treatment. The oil collecting device adopts the oil collecting tank 7. The oil collecting tank 7 is made of channel steel. There is an oil outlet weir near the oil layer. The oil outlet weir is triangular in shape. There is a circle of thin plates on the inner wall of the triangular weir. On the slideway, it can be adjusted by itself according to the thickness of the oil layer. A heating system that can be heated to different temperatures according to the change of the external temperature is designed under the oil collecting tank 7. The physical structure of the heating system is a space spiral tube heating plate. Pipe 8, sometimes the oil layer flows slowly. In order to facilitate the oil layer to be discharged to the oil collection system in time, the principle of increasing the temperature to reduce the viscosity of the oil layer is used, so that the oil layer can flow into the oil collection system more smoothly. The bottom surface of the oil collecting tank 7 near the port is designed with a slope, which is more conducive to the inflow and outflow of oil and reduces the occurrence of oil accumulation. The side wall scraping device 12 uses the same central rotating shaft, which is the same rotating shaft as the rotating shaft of the automatic frequency conversion stirring device 16. The rotating shaft is connected to the side wall scraping device through a separation mechanism and a transmission mechanism, and the separation mechanism can be used. The rotating shaft is connected or separated from the transmission mechanism, and the transmission mechanism is connected with the side wall scraping device. Using the separation mechanism, when cleaning is required, the gear and the side wall scraping device are connected, and the scrubbing intensity can be adjusted by the frequency conversion pump. Through the signal control of the console 37, the speed of the pump can be adjusted, so that the washing process is more flexible. Sampling device 9, in order to know the experimental effect, some data need to collect the mixed liquid inside the device. The natural sedimentation tank is provided with 4 sampling ports according to the different heights, and each sampling port is provided with a sampling device 9. The oil and water are in contact with each other. A sampling port is opened at the position of the subsidence, a sampling port is opened at a deeper depth, then a sampling port is set in the middle part of the settlement, and finally a sampling port is opened between the solid and liquid phases, so that according to different Sampling is carried out at different parts of the sample, and then relevant experiments are carried out. A stop valve is installed at the outlet of each sampling port. One end of the valve is connected to the sampling port, and the other end is connected to a hose, which is connected to the final container for sampling liquid. , when sampling is required, open the corresponding valve.

混凝沉降装置2中设计了一个斜板结构10,此斜板结构10是由多个塑料波纹板组合而成,波纹的作用一方面是增加与污水的接触面积,另一方面是更有利于污泥沉积,斜板的设计是采用了浅池原理,使原水分为多个层次,增加污水与斜板的接触面积,更有利含油污水的沉降,此斜板结构最终的形态是多个环形结构,开口朝上的半径大,开口朝下的半径小,简单的来看是由多个喇叭状的塑料板相间组合而成,波纹板与波纹板之间有固定连接的结构,使斜板结构10不易变形,在斜板下方放有一个支撑结构11,用来支撑整个斜板结构10,斜板的上部开有吊环,当需要进行更换或者清洗的时候,利用吊钩可以很方便地从罐的上方将其调出罐外,从而进行清洗和更换。A sloping plate structure 10 is designed in the coagulation settling device 2. The sloping plate structure 10 is composed of a plurality of plastic corrugated plates. The function of the corrugation is to increase the contact area with sewage on the one hand, and it is more conducive to the For sludge deposition, the design of the inclined plate adopts the principle of shallow pool, so that the raw water can be divided into multiple layers, which increases the contact area between the sewage and the inclined plate, which is more conducive to the sedimentation of oily sewage. The final shape of the inclined plate structure is a plurality of annular Structure, the radius of the opening facing up is large, and the radius of the opening facing down is small. In simple terms, it is composed of multiple trumpet-shaped plastic plates. There is a fixed connection structure between the corrugated plate and the corrugated plate, so that the inclined plate The structure 10 is not easily deformed. A support structure 11 is placed under the inclined plate to support the entire inclined plate structure 10. The upper part of the inclined plate is provided with a lifting ring. The top of the tank pulls it out of the tank for cleaning and replacement.

进药口与进水口相连接,是为了将从药库33出来的药物与含油污水混合,此部分安装有流量计,用来观察药物的量,压力计用来看打入的压强是否能够满足药物进入进水口的压强,电控节流阀与流量计、压力计的信号组合在一起,利用这些测量装置的参数来控制阀门开闭以及阀门开度,药库33总共有三种药物,根据不同的条件要求,由控制系统来控制阀门的开度,根据模拟的原水成分情况不同,采取不同的配比,最终调制成所需要的比例。混凝沉降装置2中同样也需要气浮装置19,由于混合液中引进了药物的作用,是混合液中成分更为复杂,粘度也会增加,所以气浮装置的采用会有利于混凝过程的沉降分离。混凝沉降装置2中也加入了自动变频搅拌装置16,使药物能较快较均匀地与含油污水混合在一起,搅拌桨的桨叶共有八片,根据原水以及药物成分的不同,搅拌桨的形状预计设计了三种,这三种的差别在于旋转角度的不同,以及叶片面积大小不同,由于这些区别,它们作用的场景就有所差别,根据搅拌速度和力度的大小从而来选取适合相应条件的搅拌桨。搅拌桨16安装在中心转动轴上,中心转动轴处于混凝沉降罐的中心位置,上端通过联轴器与带有控制系统的电动机相连,电动机安装在混凝沉降罐的上部,它的下面有一个起支撑作用的钢架结构,通过四个螺母将电动机与钢架结构旋钮在一起。The medicine inlet is connected with the water inlet to mix the medicine from the medicine store 33 with oily sewage. A flow meter is installed in this part to observe the amount of medicine, and the pressure gauge is used to check whether the injected pressure can meet the The pressure of the drug entering the water inlet, the electronically controlled throttle valve is combined with the signals of the flowmeter and pressure gauge, and the parameters of these measuring devices are used to control the valve opening and closing and the valve opening. There are three kinds of drugs in the drug store 33. According to different According to the different conditions of the simulated raw water, different ratios are adopted, and finally the required ratio is modulated. The coagulation and settling device 2 also needs an air flotation device 19. Due to the introduction of drugs into the mixed liquid, the components in the mixed liquid are more complex and the viscosity will increase, so the use of the air flotation device will be beneficial to the coagulation process. sedimentation separation. The automatic frequency conversion stirring device 16 is also added to the coagulation settling device 2, so that the medicine can be mixed with the oily sewage quickly and evenly. There are eight blades of the stirring paddle. Three shapes are expected to be designed. The difference between the three types lies in the rotation angle and the size of the blade area. Due to these differences, the scenes they act on are different. The appropriate conditions are selected according to the stirring speed and strength. stirring paddle. The stirring paddle 16 is installed on the central rotating shaft, and the central rotating shaft is in the center of the coagulation settling tank, and the upper end is connected with the motor with the control system through the coupling. A steel frame structure that acts as a support, and the motor and the steel frame structure knob are connected together by four nuts.

升压缓冲装置23包括压力计、流量计、报警装置、过滤网(底部、可定时移出清洗更换),它使上游流过来的压力和流速不稳定的混合液稳定在一个范围内,在离入口半米的位置处安装有压力与流量传感器,根据传感器返回的数据来确定混合液需要在缓冲装置的停留时间,装置底部设置了一个滤网28,再往下有一个开口,开口用来放出污泥和杂质,右端为出水口,出水口与出水管线相连,出水管线与出口相间处安装了升压装置,接着与进水口一样,安装流量和压力传感器。在缓冲装置的紧贴滤网28右侧的壁上有一个矩形的密封口,滤网28的清洗与更换可以通过洗密封口移出装置外侧。报警装置与传感器相关,如果压力和流量过大则报警装置会产生警报。The pressure boosting buffer device 23 includes a pressure gauge, a flow meter, an alarm device, and a filter screen (the bottom can be removed for cleaning and replacement at regular intervals). A pressure and flow sensor is installed at a position of half a meter. According to the data returned by the sensor, the residence time of the mixed liquid in the buffer device is determined. A filter screen 28 is set at the bottom of the device, and there is an opening at the bottom. Mud and impurities, the right end is the water outlet, the water outlet is connected with the water outlet pipeline, the pressure booster is installed between the water outlet pipeline and the outlet, and then the flow and pressure sensors are installed like the water inlet. There is a rectangular sealing opening on the wall of the buffer device close to the right side of the filter screen 28, and the cleaning and replacement of the filter screen 28 can be removed from the outside of the device through the cleaning and sealing opening. The alarm device is associated with the sensor and will generate an alarm if the pressure and flow are too high.

过滤装反冲洗装置24主要包括进水配水结构29、滤头筛网结构25、滤料层、衬托层30、集水机构29、分层分频搅拌加压冲洗装置27、污泥污垢收集区结构、反冲洗回路结构、压力报警器,滤料层更换与清洗结构。经过升压缓冲装置23的水通过滤头筛网结构25的进水配水管线进入到过滤罐中,以一定的压力洒落到滤料上层,配水管5可以围绕中轴进行缓慢匀速的旋转,这样可以使得配水更为均匀,滤头转换结构26参阅图26,滤网28参阅图28。滤料层分为三部分,从上往下粒径越来越大,首先是粒径细的细沙,接着是粒径较细的粗砂或者是别的滤料,再往下是粒径较大的砾石,砾石下方便是位于底部的支撑结构(衬托层30),支撑上方的滤料,集水机构29也同样是反冲洗时的配水结构,它由几个带开孔的管子组成,正常工作时,滤后水会经过此集水机构排出过滤罐,反冲洗时,反冲洗的水通过此集水管,以一定的压力通过小孔向上喷出完成反冲。分层分频搅拌加压冲洗装置27,在滤料层的每一层都对应有一个搅拌桨,根据每层滤料条件得不同,每层的搅拌桨的桨叶大小、个数以及倾斜角度也不同,第一层由8个,第二层6个,第三层4个,由于长时间的过滤,每层滤料都黏附很多的污垢,降低了滤料对混合液中杂质的吸附作用,为了使滤料表面更为清洁,提高过滤效果,分层分频搅拌加压冲洗装置27使得每层滤料可以充分的进行翻转、清洗以及使得大部分滤料能够参加到过滤过程中来,减少浪费,在分层分频搅拌加压冲洗装置27上还加有带有小孔的管径装置,在搅拌桨旋转的同时,洁净的清水以一定的压力通过小孔然后喷射到滤料中去,使得滤料得到进一步的清洗。污泥污垢收集结构在过滤罐的底部,底部是一个椭球形状,在此面上设计了一个洗刷头14,可以对沉积在面上的污垢进行清洁,设定一个时间段,经过这个时间段后,洗刷头14依据设定好的螺旋轨道15进行对面部的清刮,等到达底部后,洗刷头14上的污垢基于重力的作用掉入此前在底部设计的凹坑,凹坑底部开设有孔,在孔的基础上安装了一个根据压力来进行自动开合的阀门机构,等到沉积物重量达到设定的压力值之后,阀门自行打开。所述报警装置是根据过滤装置内部的压力进行设定的,在装置内部安装一个压力传感器,当内部压力过大时,此压力传感器会将此时的数据传给报警系统,报警系统由红色报警的提醒,此时就需要相关人员进行操作。The filter-mounted backwash device 24 mainly includes a water inlet water distribution structure 29, a filter head screen structure 25, a filter material layer, a backing layer 30, a water collecting mechanism 29, a layered frequency division stirring and pressure washing device 27, and a sludge and dirt collection area. Structure, backwash circuit structure, pressure alarm, filter material layer replacement and cleaning structure. The water passing through the pressure boosting buffer device 23 enters the filter tank through the water inlet and water distribution pipeline of the filter head screen structure 25, and is sprinkled on the upper layer of the filter material with a certain pressure. The water distribution pipe 5 can rotate slowly and uniformly around the central axis, so that The water distribution can be made more uniform, see FIG. 26 for the filter head conversion structure 26, and FIG. 28 for the filter screen 28. The filter material layer is divided into three parts, and the particle size is getting larger and larger from top to bottom. The first is fine sand with fine particle size, followed by coarse sand with finer particle size or other filter materials, and then down is the particle size. Larger gravel, under the gravel is the supporting structure (backing layer 30) at the bottom, supporting the filter material above, and the water collecting mechanism 29 is also the water distribution structure during backwashing, which consists of several pipes with openings , During normal operation, the filtered water will be discharged from the filter tank through this water collecting mechanism. During backwashing, the backwashed water will pass through this water collecting pipe and be ejected upward through the small hole with a certain pressure to complete the backwash. The layered and frequency-distributed stirring and pressurized washing device 27 has a corresponding stirring paddle in each layer of the filter material layer. According to the filter material conditions of each layer, the size, number and inclination angle of the paddles of each layer of stirring paddles are different. It is also different. The first layer consists of 8, the second layer is 6, and the third layer is 4. Due to long-term filtration, each layer of filter material adheres to a lot of dirt, which reduces the adsorption effect of the filter material on impurities in the mixture. , in order to make the surface of the filter material cleaner and improve the filtration effect, the layered and frequency-distributed stirring and pressure washing device 27 enables each layer of filter material to be fully turned over and cleaned, and most of the filter material can participate in the filtration process. To reduce waste, a pipe diameter device with small holes is also added to the stratified frequency division stirring and pressure washing device 27. When the stirring paddle rotates, clean water passes through the small holes with a certain pressure and is then sprayed into the filter material. to allow the filter material to be further cleaned. The sludge and dirt collection structure is at the bottom of the filter tank, and the bottom is an ellipsoid shape. A scrubbing head 14 is designed on this surface, which can clean the dirt deposited on the surface, and set a time period, after this time period After that, the scrub head 14 cleans the face according to the set spiral track 15. After reaching the bottom, the dirt on the scrub head 14 falls into the previously designed pit at the bottom based on the action of gravity. The bottom of the pit is provided with On the basis of the hole, a valve mechanism that automatically opens and closes according to the pressure is installed. After the weight of the sediment reaches the set pressure value, the valve opens by itself. The alarm device is set according to the pressure inside the filter device, and a pressure sensor is installed inside the device. When the internal pressure is too large, the pressure sensor will transmit the data at this time to the alarm system, and the alarm system will alarm by red. Reminder, at this time, the relevant personnel are required to operate.

结合图13、图14、图15所示,污泥污垢收集结构包括洗刷头14和螺旋轨道15,洗刷头可伸缩、可自转,螺旋轨道截面为矩形,洗刷头包括毛刷、洗刷头盒13,洗刷头盒内部设置正反转可控的小型电动机和控制器,洗刷头盒侧边设置两个行走轮38,洗刷头盒设置轨道孔40,螺旋轨道从轨道孔穿过,洗刷头盒可以沿着螺旋轨道滑动,螺旋轨道的起始端和末端设置位置传感器。工作过程中,洗刷头14通过小型电动机带动行走轮,轮子表面做的有比较深的凹槽,增加与过滤罐壁的摩擦力,利用轮子与过滤罐壁的摩擦力沿着穿过洗刷头的螺旋轨道进行空间的螺旋运动,从而进行正向的洗刷,螺旋轨道15是矩形条做成的,相应的洗刷头的轨道孔40也是矩形,这样做的目的是减少洗刷头的空间自由度,使得洗刷头只能沿着螺旋轨门道进行移动,不能转动,从而保证了与罐壁的垂直接触;行走轮与罐壁接触时会有间隙产生,毛刷可能因为间隙距离大而接触不到罐壁,为了解决这个问题,将洗刷头做成可伸缩的结构,在运动的过程中,洗刷头可以根据空隙的大小自由地进行调节,从而解决了刷子头接触不到罐壁的问题。由于螺旋轨道上安装有位置传感器39,当洗刷头运动至底部位置传感器时,此时传感器把信号反馈到控制系统,控制系统接收到此信号后,通过无线发射器发出指令使洗刷头内部装有无线接收器的电机进行反转,从而使洗刷头回到最初的位置,在回程的过程中又对罐底部进行了一次清洗。13, 14 and 15, the sludge and dirt collection structure includes a scrub head 14 and a spiral track 15. The scrub head is retractable and self-rotating, and the cross section of the spiral track is rectangular. The scrub head includes a brush and a scrub head box 13. , a small motor and a controller with controllable forward and reverse rotation are arranged inside the scrub head box, two walking wheels 38 are arranged on the side of the scrub head box, a track hole 40 is arranged in the scrub head box, the spiral track passes through the track hole, and the scrub head box can be Slide along the spiral track, and position sensors are set at the beginning and end of the spiral track. During the working process, the scrubbing head 14 drives the walking wheel through a small motor. The surface of the wheel has relatively deep grooves to increase the friction with the filter tank wall. The spiral track performs a spiral motion in space, so as to perform positive scrubbing. The spiral track 15 is made of rectangular strips, and the corresponding track hole 40 of the scrub head is also rectangular. The purpose of this is to reduce the spatial freedom of the scrub head, so that the The scrub head can only move along the spiral track doorway and cannot rotate, thus ensuring vertical contact with the tank wall; there will be a gap when the walking wheel contacts the tank wall, and the brush may not be able to contact the tank wall due to the large gap distance. , In order to solve this problem, the brush head is made into a retractable structure. During the movement process, the brush head can be adjusted freely according to the size of the gap, thus solving the problem that the brush head cannot contact the tank wall. Since the position sensor 39 is installed on the spiral track, when the scrub head moves to the bottom position sensor, the sensor feeds back the signal to the control system. After the control system receives the signal, it sends an instruction through the wireless transmitter to make the scrub head internally equipped with The motor of the wireless receiver reverses, which returns the scrub head to its original position, cleaning the bottom of the tank one more time on the way back.

配药装置33为药库,根据实验中需要的药剂,将药库设置了四个放置药物的空闲区,每个空闲区都是长方体的形状,每个空间的两端都开有孔,一端安装了可以自动调节大小的阀门机构,另一端与带有泵机的管路相连接,带有阀门的一端与控制电路相连,当系统中需要添加相应的药剂时,控制台37采取相应的对阀门的信号控制,控制药剂的添加,每个隔板的上下位置都安置的有液位传感器,用来对液位的监测,当液位高于最高位或者低于最低位时,液位传感器会把信号给报警系统,通知控制台采取应急措施,当液位过高时应关闭阀门,停止对药库的补加,当液位显示过低时,会加大泵机的回转速度,及时往药库添加所需要的药剂。The medicine dispensing device 33 is a medicine storehouse. According to the medicines required in the experiment, the medicine storehouse is set with four free areas for placing medicines. Each free area is in the shape of a rectangular parallelepiped. There is a valve mechanism that can automatically adjust the size, the other end is connected with the pipeline with the pump, and the end with the valve is connected with the control circuit. When the corresponding drug needs to be added to the system, the console 37 takes corresponding valve Signal control to control the addition of chemicals, a liquid level sensor is placed on the upper and lower positions of each partition to monitor the liquid level. When the liquid level is higher than the highest level or lower than the lowest level, the liquid level sensor will Send the signal to the alarm system and notify the console to take emergency measures. When the liquid level is too high, the valve should be closed to stop the replenishment of the drug store. When the liquid level is too low, the rotation speed of the pump will be increased, and the Add the medicine you need to the medicine store.

污泥污水回收装置36采用一个长方体的大铁箱,上部没有盖,底部设计成漏斗的形状,中间用隔板分开,一半用于回收污水一半用来收集污泥,锥形底部与管线相连接,锥形底部与管线通过法兰与带有压力传感器的阀门相连接,系统中的通过负压将污泥吸出,之后从顶部排到污泥收集装置中,污水通过泵机将系统各个位置处的处理后的污水同样也从上方泵回到污水收集部分中,当收集机构中的底部压力达到设定的值之后,压力传感器将信号给予底部阀门,将先前处于闭合的状态改为打开,等到污泥与污水排出一定时间后,压力减小了,传感器就会识别到当前的压力已不再满足设定的条件就会使阀门自动关闭等到下次压力再次满足条件为止。The sludge and sewage recovery device 36 adopts a large rectangular iron box, the upper part has no cover, and the bottom is designed in the shape of a funnel. , the conical bottom and the pipeline are connected to the valve with pressure sensor through the flange, the sludge in the system is sucked out by negative pressure, and then discharged from the top to the sludge collection device, and the sewage is pumped to each position of the system through the pump. The treated sewage is also pumped back to the sewage collection part from above. When the bottom pressure in the collection mechanism reaches the set value, the pressure sensor will give a signal to the bottom valve, changing the previously closed state to open, and wait until After the sludge and sewage are discharged for a certain period of time, the pressure is reduced, and the sensor will recognize that the current pressure no longer meets the set conditions, and the valve will automatically close until the next pressure meets the conditions again.

污油通过污油回收装置34进行回收,污油经过过滤网通过入口进入到污油回收罐中,罐分为三层,每层都有一个网格大小不同的滤网,使得污油在往下沉降的过程中能筛掉一部分的杂质,尽可能降低出油口处油的杂质含量,同时出油口处也包含一个滤网。每个滤网附近处都安装了一个压力传感器,相对应的也有报警装置,当某一部分滤网上的杂质过多导致此处的压力升高时,报警装置就会进行提醒,那么就需要进行更换和清洗相对应处的滤网;在收油装置的内部还设有一个从顶到底部的空间螺旋加热管线35,顶部为进热水口,底部为出热水口,由于环境的变化,有时罐中的油流动缓慢,不能满足设备的处理要求,此时通过提高油的温度,可以减小污油的粘度进而提高油的流动性。污油回收装置34长时间的使用会积累大量的油污,装置内的加热管线以及滤网通过吊环可以起吊到外部进行清洗和更换。The dirty oil is recovered by the dirty oil recovery device 34, and the dirty oil enters the dirty oil recovery tank through the inlet through the filter screen. In the process of lower settlement, part of the impurities can be screened out, and the impurity content of the oil at the oil outlet can be reduced as much as possible, and a filter screen is also included at the oil outlet. A pressure sensor is installed near each filter screen, and there is also an alarm device correspondingly. When too much impurities on a certain part of the filter screen cause the pressure here to rise, the alarm device will remind you, then it needs to be replaced. The filter screen corresponding to cleaning; there is also a space spiral heating pipeline 35 from top to bottom inside the oil collecting device. The top is the hot water inlet and the bottom is the hot water outlet. Due to changes in the environment, sometimes The oil in the tank flows slowly and cannot meet the processing requirements of the equipment. At this time, by increasing the temperature of the oil, the viscosity of the dirty oil can be reduced and the fluidity of the oil can be improved. The long-term use of the dirty oil recovery device 34 will accumulate a large amount of oil pollution, and the heating pipeline and the filter screen in the device can be lifted to the outside through the lifting ring for cleaning and replacement.

下面给出本装置作业过程:The working process of this device is given below:

步骤1:检查设备是否正常工作。Step 1: Check if the device is working properly.

步骤2:开启泵,将原水泵入到沉降环节。Step 2: Turn on the pump and pump the raw water into the sedimentation link.

步骤3:通过控制台检查速度压力是否有异常。Step 3: Check whether the speed pressure is abnormal through the console.

步骤4:等待一段之间,如果没有警报产生,则对每个环节进行采样,看是否满足标准。如果有警报或异常产生,需要先解决报警处的问题,等警报解除后再进行下一步的工作。Step 4: Between waiting periods, if no alarm is generated, sample each link to see if the criteria are met. If there is an alarm or abnormality, it is necessary to solve the problem at the alarm place first, and then proceed to the next step after the alarm is cleared.

步骤5:如果不满足标准,根据控制台收到的每一处的数据信息来分析可能产生问题的原因。根据分析的可能原因进行对相应位置的参数改变控制,例如流量小了需要调大,压力大了需要降低等,进行这些操作后,再等待一段时间采集一部分样本分析是否满足标准,如果不满足,则需要继续的分析调试,直到满足条件为止。Step 5: If the standard is not met, analyze the possible cause of the problem according to the data information received by the console. Change and control the parameters of the corresponding position according to the possible causes of the analysis, such as the flow rate needs to be increased, the pressure needs to be reduced, etc. After these operations, wait for a period of time to collect a part of the sample to analyze whether it meets the standard, if not, Continue to analyze and debug until the conditions are met.

步骤6:满足标准后,需要将每个环节的参数保留记录下来,以方便以后的工作,方便对比和考察。Step 6: After meeting the standard, it is necessary to keep and record the parameters of each link to facilitate future work and facilitate comparison and inspection.

本发明创新之处在于:The innovation of the present invention lies in:

遥控位移装置,每个体形较大的装置底部都设置的有滚轮系统,每个滚轮系统共有四个滚轮17,每横着的两个为一对,其中后两个为动力系统,剩下的两个用来控制方向,整个滚轮系统通过红外线进行信号的传递,每个装置都配有一个遥控器,进而可以方便地进行装置的安放和托运,减少了人力的成本。Remote control displacement devices, each larger device has a roller system at the bottom, and each roller system has four rollers 17, each of which is a pair. One is used to control the direction, the entire roller system transmits signals through infrared rays, and each device is equipped with a remote control, which can facilitate the placement and shipping of the device, reducing labor costs.

变频搅拌升降系统,这个系统配合沉降系统进行工作的,在传统的污水处理厂中,自然沉降一般只是依靠长时间的沉降过程,加入变频搅拌升降系统后,依据入水口速度压力传感器信号的变化,来改变搅拌装置的搅拌频率,使得含油污水在沉降前更为充分的混合,从而利于接下来的沉降过程,另外这个搅拌装置设计为可以自动升降是为了方便以后的清洗和更换。Frequency conversion stirring and lifting system, this system works in conjunction with the sedimentation system. In traditional sewage treatment plants, natural settlement generally only relies on a long-term sedimentation process. To change the stirring frequency of the stirring device, so that the oily sewage can be more fully mixed before settling, which is beneficial to the subsequent settling process. In addition, the stirring device is designed to automatically rise and fall to facilitate future cleaning and replacement.

斜板机构,根据浅池原理,将罐中的水分为更为细小的层次,增加了污水与板的接触面积,从而更加有利于沉降,实现了在同样的时间内,污水沉降的效果更加有效,斜板结构由多个锥形塑料波纹板组合而成,在其上部的两侧有耳孔用来在清洗个更换时将其调出,下部有支撑结构11,支撑结构11是镂空的,方便上方的水流出,根据沉降装置的直径大小选择适当的斜板个数,在提高效果的同时尽可能的减少成本。The inclined plate mechanism, according to the principle of shallow pool, divides the water in the tank into finer layers, which increases the contact area between the sewage and the plate, which is more conducive to settlement, and realizes that the effect of sewage settlement is more effective in the same time. , The inclined plate structure is composed of a plurality of conical plastic corrugated plates. There are ear holes on both sides of the upper part to be used for cleaning and replacement. The lower part has a supporting structure 11. The supporting structure 11 is hollow and convenient The water above flows out, and the appropriate number of inclined plates is selected according to the diameter of the settling device, so as to improve the effect and reduce the cost as much as possible.

两级沉降装置是本设计的核心,根据沉降情况实时地进行相应的操作,搅拌系统是为了使刚进入的含油污水混合的更加均匀,使得油滴与油滴、杂质与杂质之间可以形成更大的油滴和杂质,便于接下来的沉降,与传统沉降不同的是增加了清洗换洗结构,装置长时间的工作各个部分必然会积累大量的污垢,自动清洗装置能够对搅拌系统、沉降侧壁以及底部进行定期的刮洗,从而可以提高工作效果。The two-stage sedimentation device is the core of the design, and the corresponding operations are carried out in real time according to the sedimentation situation. The stirring system is to make the oily sewage that has just entered more evenly mixed, so that oil droplets and oil droplets, impurities and impurities can form more evenly. Large oil droplets and impurities are convenient for subsequent sedimentation. Different from traditional sedimentation, a cleaning and washing structure is added. A large amount of dirt will inevitably accumulate in various parts of the device during long-term operation. The automatic cleaning device can clean the stirring system and sedimentation sidewall. And the bottom is regularly scraped, which can improve the working effect.

进水配水、集水出水等流速压力,每个进水口和出水口都设置的有自动控制的电控阀门,由于人工操作总是精度有限,而且一般都会有延迟,采用电控阀门可以有效地解决上述问题,控制台根据相应进水口出水口流量压力传感器回传的信号,进行对相应位置处电动阀门状态以及阀门开度等的控制,从而提高了整个系统的自动化水平。The flow rate and pressure of water inlet and water distribution, water collection and outlet water, etc., each water inlet and outlet is equipped with an automatically controlled electronically controlled valve. Due to the limited accuracy of manual operation, and there is usually a delay, the use of electronically controlled valves can effectively To solve the above problems, the console controls the state of the electric valve at the corresponding position and the valve opening according to the signal returned by the flow pressure sensor at the corresponding water inlet and outlet, thereby improving the automation level of the entire system.

配药装置33采用上线限位信号控制的自动系统,由控制台得知每个环节处药物的添加情况,例如添加的药剂少,可能加药某一部分压强小需要增压,而有的部分加药过多,应该此处的压强过大需要减小压力;另外,药库自身也需要定时的补加相应的药剂。根据每个加药位置处的传感器信号进行流量压力的控制,药库自身采用上下限位的压力传感器来感知药库中的药是否已经填满或不够。The dispensing device 33 adopts an automatic system controlled by an on-line limit signal, and the console knows the addition of medicines at each link. For example, if there are few medicines added, a certain part of the medicine may have a low pressure and need to be pressurized, while some parts are filled with medicine. If it is too much, the pressure here should be too high and the pressure needs to be reduced; in addition, the drug store itself also needs to be supplemented with corresponding drugs regularly. The flow pressure is controlled according to the sensor signal at each dosing position, and the drug store itself uses pressure sensors with upper and lower limits to sense whether the drug in the drug store has been filled or not enough.

过滤反冲洗装置24中的配水系统与传统固定结构不同,本发明中的配水系统依靠自身的力偶作用,可以是配水系统围绕中轴进行缓慢匀速的旋转,进而来解决配水有死角不均匀等问题;本发明采用分层变频搅拌装置,滤料分为三层,各层之间都有一个能进行分割的板状结构,由于长时间的过滤,滤料的表层会积累大量的污垢杂质,并且有的滤料可能参与不到过滤的过程中去,为了能够使更多的滤料参与到过滤环节中,搅拌装置就起到很好的作用,由于每层滤料的结构成分不一样,所以采取分层搅拌并且根据不同速度配比来找到最佳的速度匹配。The water distribution system in the filter backwash device 24 is different from the traditional fixed structure. The water distribution system in the present invention relies on its own force couple, and the water distribution system can rotate slowly and uniformly around the central axis, thereby solving the problem of uneven dead corners in the water distribution. The invention adopts a layered variable frequency stirring device, the filter material is divided into three layers, and there is a plate-like structure that can be divided between each layer. Some filter materials may not participate in the filtration process. In order to allow more filter materials to participate in the filtration process, the stirring device plays a very good role. Since the structural components of each layer of filter materials are different, so Take layered stirring and find the best speed match according to different speed ratios.

本发明通过一次沉降装置来模拟实际的自然沉降效果,通过加药环节,实现二次混凝沉降的效果,可以调整打入量的参数来实时进行控制药剂添加的多少,进而实现更加精准的控制。在运输方面,本发明设置了电动滚轮,不通电的情况下也可人力推动,配合电动滚轮的有遥控器,通过电控可以很方便的实现装置的位置改变,使整个系统的安装更为方便。为了方便维修和清洗,在每个装置都预留的有可以通过吊车挂起的地方,起吊装置18参阅图18,同时有的部位通过自动升降装置,使容易积垢的部位显露出来,然后进行清洗。通过过滤反冲洗装置24进行对实际过滤反冲的模拟,通过安插在各个模拟装置的传感器,传感器类型比较多,主要包含有流量传感器、压力传感器、温度传感器、pH值传感器、悬浮物浓度传感器、悬浮物粒径传感器,测定含油量的传感器等,来得知污水处理的效果,进而可以凭借这些参数来进行相关环节的调试,直至达到回注水或者外排水的标准。整个装置系统的控制根据各个传感器测到的实时数据,根据回传的数据控制相应位置处的阀门开度、药剂的打入力度和药量的多少,通过控制台来进行对整个装置的控制,各个位置的数据通过数据采集系统回传给上位机。为了进一步地方便监控污水处理情况,本发明还采用无线传输技术,由于整个模拟系统是在一个范围比较小的空间,所以无线传输技术的实现是可行的,而且传输速度也很快,系统给一个信号,相应的机构会很快地做出响应,这样避免了延迟的问题。在控制技术方面,可以通过控制台的主机来进行对整个装置系统的控制。另外,为了实现进一步地自动化,能够在远程就能监控整个系统的运作,本发明中还设计了与此处理系统紧密相连的手机APP,用户可以通过这个手机客户端方便地了解到整个系统的运行情况,而且在这个APP中还提供警报系统,当整个系统装置出现异常情况时,系统会将异常状况上传到手机客户端,及时的提醒客户有紧急状况需要处理。The present invention simulates the actual natural settlement effect through the primary settling device, and realizes the effect of secondary coagulation settling through the drug addition link, and the parameters of the injection amount can be adjusted to control the amount of the medicament added in real time, thereby realizing more precise control. . In terms of transportation, the present invention is provided with an electric roller, which can be pushed manually even when the power is not turned on. The remote controller is equipped with the electric roller, and the position of the device can be easily changed through the electric control, which makes the installation of the whole system more convenient. . In order to facilitate maintenance and cleaning, there is a place reserved for each device that can be hung by a crane. The lifting device 18 is shown in Figure 18. At the same time, some parts are exposed by the automatic lifting device to expose the parts that are prone to fouling, and then carry out cleaning. The simulation of the actual filter backflush is carried out through the filter backwash device 24, and there are many types of sensors installed in each simulation device, mainly including flow sensors, pressure sensors, temperature sensors, pH sensors, suspended solids concentration sensors, Suspended matter particle size sensor, sensor for measuring oil content, etc., to know the effect of sewage treatment, and then we can use these parameters to debug related links until it reaches the standard of re-injection or external drainage. The control of the entire device system is based on the real-time data measured by each sensor, and the valve opening at the corresponding position, the injection force of the drug and the amount of the drug are controlled according to the returned data, and the entire device is controlled through the console. The data of each position is sent back to the upper computer through the data acquisition system. In order to further facilitate the monitoring of sewage treatment, the present invention also adopts wireless transmission technology. Since the entire simulation system is in a relatively small space, the realization of wireless transmission technology is feasible, and the transmission speed is also very fast. signal, the corresponding agency will respond quickly, thus avoiding the problem of delay. In terms of control technology, the entire device system can be controlled through the host of the console. In addition, in order to realize further automation and be able to monitor the operation of the entire system remotely, the present invention also designs a mobile phone APP that is closely connected with the processing system, and the user can easily understand the operation of the entire system through the mobile phone client When there is an abnormal situation in the whole system device, the system will upload the abnormal situation to the mobile phone client, and timely remind the customer that there is an emergency situation that needs to be dealt with.

Claims (10)

1. The utility model provides an oil field produced water handles simulation experiment device which characterized in that: the oilfield produced water treatment simulation experiment device comprises a raw water preparation device, a natural sedimentation device (1), a coagulation sedimentation device (2), a boosting buffer device (23), a filtering backwashing device (24), a dispensing device (33), a sump oil recovery device (34), a sludge and sewage treatment device (36), an automatic cleaning device, a remote control displacement device, an alarm device and a control console (37), wherein the natural sedimentation device (1) comprises a natural sedimentation tank, a water inlet and distribution structure, a water collecting structure, an oil collecting structure, a water drainage structure and a sludge treatment structure are arranged in the natural sedimentation tank, the water inlet and distribution structure comprises a water inlet part and a water distribution part, an electric control valve is arranged at a water inlet of the water inlet part, the flow rate and the flow rate of inlet water are controlled, and a flowmeter and a pressure gauge are arranged around the electric control valve; the water distribution part is provided with a plurality of water distribution ports, each water distribution port is provided with an electric control valve, each water distribution port is provided with a filter head, the filter head is connected with an automatic assembling and disassembling device, the automatic assembling and disassembling device is used for transferring the filter head which is fully covered with dirt to a cleaning area for cleaning, then the filter head is returned to the water distribution port for re-installation, and the flow of the water distribution part is controlled in real time on a console system interface according to data transmitted by a flow velocity sensor and a pressure sensor; the water distribution part is provided with an automatic frequency conversion stirring device, and the stirring frequency of the stirring device is changed according to the change of the water inlet speed and the signal of the pressure sensor, so that the oily sewage is fully mixed before sedimentation; a sludge collecting port is formed at the bottom of the settling tank and is connected with a negative pressure suction system; a side wall washing and scraping device (12) is arranged above the natural settling tank, the side wall washing and scraping device (12) is connected with the automatic lifting assembly, and the side wall washing and scraping device (12) is conveyed to the bottom of the natural settling tank by the automatic lifting assembly to be washed; a throttling speed-regulating electric control valve is arranged on the water outlet pipeline; an air floatation device is arranged below the natural settling tank and arranged on a supporting frame structure, pulleys (21) are arranged on two side edges of the supporting frame structure, the pulleys (21) are in contact with rails, and the rails are arranged on two sides close to the tank wall; the oil collecting structure is an oil collecting tank (7), a circle of oil outlet weir is arranged near an oil layer of the oil collecting tank (7), the oil outlet weir is triangular, a circle of thin plate is arranged on the inner wall of the oil outlet weir, the thin plate is arranged on a slideway, a circle of heating coil (8) is arranged at the bottom of the oil collecting tank, and the bottom surface of the oil collecting tank is provided with a slope; the natural settling tank is provided with 4 sampling ports from top to bottom, each sampling port is provided with a sampling device (9), the position where oil and water are contacted is provided with one sampling port, the lower deeper part is provided with one sampling port, the middle part of the natural settling tank is provided with one sampling port downwards, finally, a solid-liquid interphase position is provided with one sampling port, the outlet of each sampling port is provided with a stop valve, the other end of each stop valve is connected with a hose, and the hose is connected with a sampling container;
the coagulation sedimentation device (2) is provided with one more inclined plate structure (10) than the natural sedimentation device (1), the inclined plate structure (10) is formed by combining a plurality of plastic corrugated plates, each plastic corrugated plate is horn-shaped, the plurality of plastic corrugated plates are alternately combined layer by layer from inside to outside, a fixedly connected structure is arranged between every two adjacent plastic corrugated plates, the inclined plates are arranged on the supporting structure (11), and the upper parts of the inclined plates are provided with hanging rings;
the boosting buffer device (23) comprises a cylinder, an alarm device and a filter screen, wherein the filter screen is detachably arranged at the bottom of the boosting buffer device, a sewage discharge outlet is arranged below the filter screen, the boosting buffer device (23) enables mixed liquid with unstable pressure and unstable flow velocity flowing upstream to be stabilized within a range, a pressure sensor and a flow sensor are arranged at a position half meter away from the inlet of the cylinder, the right end of the cylinder is provided with an outlet, the outlet is connected with a water outlet pipeline, the boosting device is arranged at the position where the water outlet pipeline and the outlet are alternated, and the outlet is also provided with the flow sensor and; a rectangular sealing opening is formed in the side wall, close to the filter screen, of the barrel, and the filter screen (28) is cleaned and replaced and is moved out of the barrel through the cleaning sealing opening; determining the retention time of the mixed liquid in the buffer device according to the data transmitted by the pressure sensor and the flow sensor, and if the pressure and the flow are overlarge, generating an alarm by the alarm device;
the filtering and backwashing device comprises a filtering tank, a water inlet and distribution device, a filter head screen structure (25), a filter material layer, a backing layer (30), a water collecting mechanism (29), a layered frequency division stirring and pressurizing flushing device (27), a sludge dirt collecting structure (13), a backwashing loop structure and a pressure alarm, wherein the filter material layer is replaced and cleaned; the layered frequency division stirring and pressurizing flushing device (27) is characterized in that each layer of the filter material layer is correspondingly provided with a stirring paddle, the size, the number and the inclination angle of each layer of the stirring paddles are different, the stirring paddles are provided with pipe diameter devices with small holes, and clean clear water passes through the small holes at a certain pressure and then is sprayed into the filter material when the stirring paddles rotate, so that the filter material is further cleaned; the sludge and dirt collecting structure (13) is arranged at the bottom of the filter tank, the bottom of the filter tank is in an ellipsoidal shape, a pit is formed in the bottom of the filter tank, a valve mechanism which can be automatically opened and closed according to pressure is installed at the bottom of the pit, the washing head (14) is arranged close to the ellipsoidal surface, the washing head (14) is used for scraping the ellipsoidal surface according to a set spiral track, after the bottom is reached, dirt on the washing head falls into the pit based on the action of gravity, and after the weight of sediment reaches a set pressure value, the valve mechanism is automatically opened.
2. The oilfield produced water treatment simulation experiment device of claim 1, wherein: the control console (37) is connected with a mobile phone APP through a network.
3. The oilfield produced water treatment simulation experiment device of claim 2, wherein: the dispensing device is provided with a plurality of vacant areas for placing medicines through partition plates, each vacant area is in a cuboid shape, two ends of each vacant area are provided with holes, an automatic adjusting valve is installed at one end of each vacant area, the other end of each vacant area is connected with a pipeline with a pump, the automatic adjusting valves are connected with a control circuit, and a control console (37) controls the addition of a certain medicine through corresponding automatic adjusting valves; the upper and lower positions of each partition plate are provided with liquid level sensors for monitoring the liquid level, when the liquid level is higher than the highest position or lower than the lowest position, the liquid level sensors can send signals to an alarm system to inform a control console (37) to take emergency measures, when the liquid level is too high, an automatic regulating valve is closed to stop adding the medicine storehouse, and when the liquid level is displayed to be too low, the rotation speed of a pump machine can be increased, and required medicines can be added into the medicine storehouse in time.
4. The oilfield produced water treatment simulation experiment device of claim 3, wherein: the sludge sewage treatment device (36) adopts an open cuboid big iron box, the bottom of the sludge sewage treatment device is designed into a funnel shape, the middle of the sludge sewage treatment device is separated by a partition plate to form a sludge pond and a sewage pond, the conical bottom of the sludge sewage treatment device is connected with a pipeline, and the conical bottom of the sludge sewage treatment device is connected with a valve with a pressure sensor through a flange.
5. The oilfield produced water treatment simulation experiment device of claim 4, wherein: the dirty oil recovery device (34) is a dirty oil recovery tank, the tank body is divided into three layers, each layer is provided with a filter screen with different grid sizes, so that a part of impurities are screened off in the process of downward sedimentation of dirty oil, the oil outlet also comprises a filter screen, a pressure sensor and an alarm device are arranged near each filter screen, and when the pressure of a certain part of the filter screens is increased due to excessive impurities on the certain part of the filter screens, the alarm device reminds the replacement and cleaning of the filter screens at the part of the filter screens; the inner wall of the tank body is provided with a spiral heating pipeline from top to bottom, the top is provided with a hot water inlet, and the bottom is provided with a hot water outlet.
6. The oilfield produced water treatment simulation experiment device of claim 5, wherein: the lateral wall wash and scrape axis of rotation that device (12) utilized automatic frequency conversion agitating unit (16) to drive, the axis of rotation passes through separating mechanism, drive mechanism and connects the lateral wall and wash and scrape the device, utilize separating mechanism, when wasing, wash the axis of rotation and scrape device (16) through drive mechanism and lateral wall and connect, wash intensity and adjust through the inverter pump, signal control through control cabinet (37) is adjusted the speed size of inverter pump, the transfer axle sets up elevating gear.
7. The oilfield produced water treatment simulation experiment device of claim 6, wherein: the sludge dirt collecting structure comprises a washing head (14) and a spiral track (15), the washing head is telescopic and can rotate, the cross section of the spiral track is rectangular, the washing head (14) comprises a brush and a washing head box (13), a small motor and a washing controller which can control forward and reverse rotation are arranged in the washing head box, two walking wheels (38) are arranged on the side edge of the washing head box, track holes (40) are formed in the washing head box (13), the spiral track (15) penetrates through the track holes (40), the washing head box (13) is in sliding connection with the spiral track (15), and a starting end and a tail end of the spiral track are provided with position sensors (39).
8. The oilfield produced water treatment simulation experiment device of claim 7, wherein: the water distribution pipe of the water inlet and distribution device slowly rotates around the central shaft at a constant speed.
9. The oilfield produced water treatment simulation experiment device of claim 8, wherein: the filter material layer of the filtering and backwashing device (24) is divided into three parts, the grain diameter is larger and larger from top to bottom, the filter material on the uppermost layer is fine sand with fine grain diameter, the filter material on the middle layer is coarse sand with fine grain diameter, the filter material on the lowermost layer is gravel with larger grain diameter, the lining layer is arranged below the gravel, and the lining layer (30) supports the filter material layer.
10. The oilfield produced water treatment simulation experiment device of claim 9, wherein: the layering frequency division stirring pressurization washing unit (27) at the three-layer stirring rake, the superiors' stirring rake has 8 paddles, the middle second floor stirring rake has 6 paddles, the third layer stirring rake has 4 paddles.
CN202010539405.8A 2020-06-14 2020-06-14 Oil field extraction water treatment simulation experiment device Expired - Fee Related CN111646595B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010539405.8A CN111646595B (en) 2020-06-14 2020-06-14 Oil field extraction water treatment simulation experiment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010539405.8A CN111646595B (en) 2020-06-14 2020-06-14 Oil field extraction water treatment simulation experiment device

Publications (2)

Publication Number Publication Date
CN111646595A true CN111646595A (en) 2020-09-11
CN111646595B CN111646595B (en) 2023-03-31

Family

ID=72345420

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010539405.8A Expired - Fee Related CN111646595B (en) 2020-06-14 2020-06-14 Oil field extraction water treatment simulation experiment device

Country Status (1)

Country Link
CN (1) CN111646595B (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113341723A (en) * 2021-06-18 2021-09-03 中海油能源发展股份有限公司采油服务分公司 FPSO adds quantity control system with intelligent chemical agent
CN115779499A (en) * 2022-12-13 2023-03-14 安徽天健生物环保股份有限公司 Deslagging device and method for oily sewage, and three-phase separation equipment and method
CN115893692A (en) * 2021-08-04 2023-04-04 中国石油天然气集团有限公司 A three-dimensional device and process for produced water treatment
NL2034834A (en) * 2023-05-15 2023-06-22 Hunan Sanxiang Sihai Water Co Ltd An Intelligent Water Treatment Detection System Based on Big Data

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201317707Y (en) * 2008-11-11 2009-09-30 大连恒基新润水务有限公司 Aeration biological filtering pool with three layers of filtering
CN102253176A (en) * 2011-05-06 2011-11-23 陕西睿海丽君环境科技有限公司 Novel oil field produced water online monitoring system
CN104984681A (en) * 2015-07-21 2015-10-21 镇江市建科工程质量检测中心有限公司 Stirring device
CN106493896A (en) * 2016-11-30 2017-03-15 苏州恒昇海绵机械制造有限公司 A kind of sponge bubbling machine with clean-out opening shaft
CN208013201U (en) * 2018-03-26 2018-10-26 中国石油化工股份有限公司 Simulate produced water treatment process testing device
CN208839110U (en) * 2018-07-30 2019-05-10 广州汉智力文环保科技有限公司 A kind of quartz filter
CN209362470U (en) * 2018-08-28 2019-09-10 扬州市立达树脂有限公司 A kind of reaction kettle for producing coating additive and being convenient for cleaning

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201317707Y (en) * 2008-11-11 2009-09-30 大连恒基新润水务有限公司 Aeration biological filtering pool with three layers of filtering
CN102253176A (en) * 2011-05-06 2011-11-23 陕西睿海丽君环境科技有限公司 Novel oil field produced water online monitoring system
CN104984681A (en) * 2015-07-21 2015-10-21 镇江市建科工程质量检测中心有限公司 Stirring device
CN106493896A (en) * 2016-11-30 2017-03-15 苏州恒昇海绵机械制造有限公司 A kind of sponge bubbling machine with clean-out opening shaft
CN208013201U (en) * 2018-03-26 2018-10-26 中国石油化工股份有限公司 Simulate produced water treatment process testing device
CN208839110U (en) * 2018-07-30 2019-05-10 广州汉智力文环保科技有限公司 A kind of quartz filter
CN209362470U (en) * 2018-08-28 2019-09-10 扬州市立达树脂有限公司 A kind of reaction kettle for producing coating additive and being convenient for cleaning

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
孙东方: "立式沉降罐分离特性研究及结构优化", 《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》 *
徐友江等: "油田注水模拟系统的数据采集与控制系统", 《化工自动化及仪表》 *
燕红等: "中原油田污水处理系统水质达标治理技术", 《油气田地面工程》 *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113341723A (en) * 2021-06-18 2021-09-03 中海油能源发展股份有限公司采油服务分公司 FPSO adds quantity control system with intelligent chemical agent
CN113341723B (en) * 2021-06-18 2022-05-20 中海油能源发展股份有限公司采油服务分公司 FPSO adds quantity control system with intelligent chemical agent
CN115893692A (en) * 2021-08-04 2023-04-04 中国石油天然气集团有限公司 A three-dimensional device and process for produced water treatment
CN115893692B (en) * 2021-08-04 2025-01-17 中国石油天然气集团有限公司 A three-dimensional device and process for producing water treatment
CN115779499A (en) * 2022-12-13 2023-03-14 安徽天健生物环保股份有限公司 Deslagging device and method for oily sewage, and three-phase separation equipment and method
NL2034834A (en) * 2023-05-15 2023-06-22 Hunan Sanxiang Sihai Water Co Ltd An Intelligent Water Treatment Detection System Based on Big Data

Also Published As

Publication number Publication date
CN111646595B (en) 2023-03-31

Similar Documents

Publication Publication Date Title
CN111646595B (en) Oil field extraction water treatment simulation experiment device
CN110496434B (en) Sand and scale removal device and implementation method in anaerobic treatment system of landfill leachate
CN209848401U (en) Sewage treatment sedimentation tank
CN118512964B (en) A contaminated groundwater treatment device with a self-adjusting function
CN202155083U (en) Intelligent driving type mud scraper
CN114653135A (en) Short-process quick separating and purifying device for turbid circulating water and purifying method thereof
CN119565240A (en) Bridge pile foundation excavation mud separation purifier
CN201752601U (en) Fiber-filter-cloth rotary disc filter device
CN204661358U (en) A kind of food and drink waste water automatic oil-separation discharge equipment
CN109453546A (en) A kind of high-efficiency thickener
CN216073299U (en) An integrated sewage treatment device
CN201997169U (en) Sewage treatment turntable-type filter tank
CN111013246A (en) Anti-pollution energy-saving filtering device and method for oilfield produced water
CN210933949U (en) Sand filter for oil production well
CN205965158U (en) Active sand filter
CN107043176A (en) Relay-type food and drink waste water exhaust apparatus
CN201737941U (en) Chain scraping methane project desanding device
CN214763812U (en) Sewage slag-dragging grid machine and sewage treatment system
CN105501717A (en) Automatic tank bottom blowdown system
CN106186109B (en) A kind of grid pond tobacco wastewater suspended substance collects separate tank
CN212039172U (en) Continuous sand flowing filter
CN117339306A (en) Fiber ball filter equipment
CN209975493U (en) A waterwheel type river duckweed cleaning equipment
CN216689711U (en) Pre-buried formula inspection shaft to food and beverage trade
CN223879598U (en) A wastewater treatment scum removal device

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20230331