技术领域technical field
本发明涉及本发明涉及一种絮凝剂回收式废油再生集成装置及其应用，属于废物资源化利用领域。The present invention relates to a flocculant recovery type waste oil regeneration integrated device and its application, belonging to the field of waste resource utilization.
背景技术Background technique
我国钢铁行业每年产生大量的废油，这些废油往往劣化程度不高，经过简单的处理即可循环使用。虽然在世界范围内废油回收工艺的研究早已开展并使用，但目前国内尚未研究出一套针对于钢铁企业废油的再生处理工艺。因此，钢铁企业每年产生的大量废油不能得到有效的合理回收，不仅造成了石油资源的大量浪费，而且造成了环境污染。my country's iron and steel industry produces a large amount of waste oil every year. These waste oils are often not highly deteriorated and can be recycled after simple treatment. Although the research on waste oil recycling technology has been carried out and used in the world, a set of regeneration treatment technology for waste oil in iron and steel enterprises has not been researched in China at present. Therefore, a large amount of waste oil produced by iron and steel enterprises every year cannot be effectively and reasonably recovered, which not only causes a large waste of oil resources, but also causes environmental pollution.
近年来，国内也出现一些较为先进的废油处理工艺，逐渐将减压蒸馏，溶剂精制与白土工艺相结合。蒸馏酸洗—白土精制工艺，其原料容易获得，投资成本较低，工艺流程较为简单，适用于多种类型的润滑油再生的优势，使得国内大部分厂家均使用该工艺，但硫酸精制时产生的酸渣难以处理，同时产生气体SO2对环境污染大，并对设备造成腐蚀。CN103194308 A公开了一种利用废油制备再生基础油的方法，该方法将废油依次通过一级过滤、二级过滤、三级过滤、雾化脱水、吸附脱色的设备。采用该方法废油的过滤速度快、效率高、不易堵塞，但是该方法仅适用于劣化程度很低的废油，对于钢铁企业产生的废油，经过该步骤处理往往达不到理想的效果。CN 102977989 A公开了一种废润滑油循环回收再生生产工艺，该工艺生产效率高、产品特性稳定、无二次污染，但往往全套设备造价昂贵，且设备移动安装不便捷。因此，上述工艺均无法满足钢铁企业对于废油处理的需要。In recent years, some more advanced waste oil treatment processes have emerged in China, gradually combining vacuum distillation, solvent refining and clay process. Distillation pickling - white clay refining process, the raw materials are easy to obtain, the investment cost is low, the process flow is relatively simple, and the advantages of being suitable for the regeneration of various types of lubricating oils make most domestic manufacturers use this process, but sulfuric acid refining produces The acid slag is difficult to deal with, and at the same time, the gas SO2 is produced, which pollutes the environment and causes corrosion to the equipment. CN103194308 A discloses a method for preparing regenerated base oil from waste oil. In the method, the waste oil is sequentially passed through equipment for primary filtration, secondary filtration, tertiary filtration, atomization dehydration, and adsorption decolorization. The filtration speed of the waste oil is fast, the efficiency is high, and it is not easy to be blocked by this method. However, this method is only applicable to the waste oil with a low degree of deterioration. For the waste oil produced by iron and steel enterprises, the ideal effect is often not achieved after this step. CN 102977989 A discloses a production process for recycling waste lubricating oil. The process has high production efficiency, stable product characteristics, and no secondary pollution. However, the cost of a complete set of equipment is often high, and the equipment is not convenient to move and install. Therefore, none of the above processes can meet the needs of iron and steel enterprises for waste oil treatment.
发明内容Contents of the invention
发明目的：本发明针对钢铁行业中废油种类多、劣化程度不高等特点，设计一种絮凝剂回收式废油再生集成装置及其应用，有针对性地实现废油回收再生，具有便捷、安全、环保的特点。该装置及处理方法在将废润滑油处理到达到国家规定标准的前提下，把废油处理所需设备集成为一套可移动的废油回收再生装置，减少废润滑油处理设备的占地面积。并实现絮凝剂的实时回收循环利用，在减少投资成本的同时增加运行效率。Purpose of the invention: Aiming at the characteristics of many types of waste oil and low degree of deterioration in the iron and steel industry, the present invention designs a flocculant recovery type waste oil regeneration integrated device and its application, and realizes waste oil recovery and regeneration in a targeted manner, which is convenient and safe , Environmental protection features. The device and treatment method integrate the equipment required for waste oil treatment into a set of mobile waste oil recovery and regeneration device under the premise of treating the waste lubricating oil up to the national standard, reducing the footprint of the waste lubricating oil treatment equipment . And realize the real-time recovery and recycling of the flocculant, increase the operating efficiency while reducing the investment cost.
技术方案：为了解决上述技术问题，本发明所采用的技术方案为：一种絮凝剂回收式废油再生集成装置，该装置主要包括废油回收装置箱体、在废油回收装置箱体内部设置的搅拌沉降罐和通过连通阀连接的蒸馏罐，所述搅拌沉降罐的上端一侧设有进油阀和与进油阀相连的废油流量计，所述搅拌沉降罐的上端另一侧设有进絮凝剂阀和与进絮凝剂阀相连的絮凝剂流量泵，所述搅拌沉降罐左侧上端设有高温蒸汽出口阀和左侧下端设有高温蒸汽进口阀，所述搅拌沉降罐右侧下端设有水渣阀以及与水渣阀相连的水渣分离器；所述蒸馏罐上端一侧设有絮凝剂回收阀和与絮凝剂回收阀相连的冷凝管，所述冷凝管的另一端与絮凝剂流量泵相连，所述蒸馏罐上端另一侧设有真空泵阀以及与真空泵阀相连的真空泵，所述蒸馏罐的下侧设有再生油阀。Technical solution: In order to solve the above technical problems, the technical solution adopted in the present invention is: a flocculant recovery type waste oil regeneration integrated device, which mainly includes a waste oil recovery device box, and is installed inside the waste oil recovery device box The stirring and settling tank and the distillation tank connected by a communication valve, the upper end of the stirring and settling tank is provided with an oil inlet valve and a waste oil flow meter connected with the oil inlet valve, and the other side of the upper end of the stirring and settling tank is provided with There is a flocculant inlet valve and a flocculant flow pump connected to the flocculant inlet valve. The upper left end of the stirring and settling tank is provided with a high-temperature steam outlet valve and the lower left end is provided with a high-temperature steam inlet valve. The right side of the stirring and settling tank is The lower end is provided with a water slag valve and a water slag separator connected with the water slag valve; the upper end of the distillation tank is provided with a flocculant recovery valve and a condensation pipe connected with the flocculant recovery valve, and the other end of the condensation pipe is connected to the The flocculant flow pump is connected, the other side of the upper end of the distillation tank is provided with a vacuum pump valve and a vacuum pump connected with the vacuum pump valve, and the lower side of the distillation tank is provided with a regeneration oil valve.
所述搅拌沉降罐的内部设有水蒸汽管道和位于蒸汽管道上方的废油过滤网。The interior of the stirring and settling tank is provided with a steam pipeline and a waste oil filter screen located above the steam pipeline.
废油回收装置箱体主要放置搅拌沉降罐和蒸馏罐并通过连通阀连接。废油在进油阀的调节下通过废油流量计和过滤网的初步过滤后进入搅拌沉降罐。絮凝剂在进絮凝剂阀和絮凝剂流量泵的作用下进入搅拌沉降罐。搅拌沉降罐底部与水渣分离器通过水渣阀相连接。高温蒸汽分别在高温蒸汽进出口阀门的控制为通过间壁换热的方式为搅拌沉降罐提供热量。真空泵与蒸馏罐上部通过真空泵阀相连接，冷凝管与蒸馏罐上部通过絮凝剂回收阀相连接。再生润滑油通过蒸馏罐底部，在再生油阀的控制下，最后流入再生油罐进行储存使用。The box of the waste oil recovery device mainly houses the stirring settling tank and the distillation tank and is connected through a communication valve. Under the regulation of the oil inlet valve, the waste oil enters the stirring and settling tank after being preliminarily filtered by the waste oil flow meter and the filter screen. The flocculant enters the stirring and settling tank under the action of the flocculant inlet valve and the flocculant flow pump. The bottom of the stirring settling tank is connected with the slag separator through the slag valve. The high-temperature steam is controlled at the high-temperature steam inlet and outlet valves to provide heat for the stirring and settling tank through the heat exchange of the partition wall. The vacuum pump is connected to the upper part of the distillation tank through a vacuum pump valve, and the condensation pipe is connected to the upper part of the distillation tank through a flocculant recovery valve. The regenerated lubricating oil passes through the bottom of the distillation tank, under the control of the regenerated oil valve, and finally flows into the regenerated oil tank for storage and use.
所述的搅拌沉降罐为圆柱结构，高度H1为1.5-2m，直径D1为0.4-0.6m，高温蒸汽进口阀相连的水蒸气管道的直径D2为0.1-0.2m，水渣阀相连的水渣管的直径D3为0.02-0.05m，进油阀相连的进油管的直径D4为0.05-0.1m，进絮凝剂阀相连的进絮凝剂管的直径D5为0.05-0.1m，与连通阀相连的出油管的直径D6为0.1-0.15m，沉降罐底部倾斜角θ为3-5°。The stirring and settling tank is a cylindrical structure, the height H1 is 1.5-2m, the diameter D1 is 0.4-0.6m, the diameter D2 of the steam pipeline connected to the high-temperature steam inlet valve is 0.1-0.2m, and the water slag valve connected to the water slag The diameter D3 of the pipe is 0.02-0.05m. The diameter D4 of the oil inlet pipe connected to the oil inlet valve is 0.05-0.1m. The diameter D5 of the flocculant inlet pipe connected to the flocculant valve is 0.05-0.1m. The diameter D6 of the oil outlet pipe is 0.1-0.15m, and the inclination angle θ at the bottom of the settling tank is 3-5°.
所述水蒸气管道的进口位于圆柱高度0.2H1处，出口位于0.8H1处，连通阀相连的出油管位于圆柱高度0.3H1处。The inlet of the steam pipeline is located at the cylinder height of 0.2H1, the outlet is located at the cylinder height of 0.8H1, and the oil outlet pipe connected with the connecting valve is located at the cylinder height of 0.3H1.
所述在废油分级回收利用装置，由真空泵提供动力，确保废油在整个过程中进行流动。通过阀门控制各组分流量和开关可以确保搅拌沉降罐和蒸馏罐的单独运行或者组合运行。The waste oil graded recycling device is powered by a vacuum pump to ensure that the waste oil flows throughout the process. Controlling the flow and switch of each component through valves can ensure the separate operation or combined operation of the stirring and settling tank and the distillation tank.
所述废油回收装置箱体为可移动的箱体。The box body of the waste oil recovery device is a movable box body.
所述废油回收装置箱体底部设有两个或两个以上的滚轮。Two or more rollers are arranged at the bottom of the box of the waste oil recovery device.
所述的一种絮凝剂回收式废油再生集成装置在回收钢铁行业中废油方面的应用。The application of the flocculant recovery type waste oil regeneration integrated device in the recovery of waste oil in the iron and steel industry.
所述的应用，即絮凝剂回收式废油再生方法，包括以下步骤：The application, i.e. flocculant recovery type waste oil regeneration method, comprises the following steps:
1）打开进油阀、连通阀和真空泵阀，关闭其他阀门，由真空泵提供动力，采用将经过静止沉降后的废润滑油上层油液通过废油流量计，将体积V0为0.25m3的废油送入搅拌沉降罐中，并在搅拌沉降罐上部通过废油过滤网时完成初步过滤；1) Open the oil inlet valve, connecting valve and vacuum pump valve, close other valves, and use the power of the vacuum pump to pass the upper layer of waste lubricating oil after static settlement through the waste oil flowmeter, and pass the waste oil with a volume V0 of 0.25m3 The oil is sent into the stirring and settling tank, and the preliminary filtration is completed when the upper part of the stirring and settling tank passes through the waste oil filter;
2）打开进絮凝剂阀，关闭其余阀门，打开絮凝剂流量泵，当絮凝剂进量达到3-5V0时关闭絮凝剂流量泵；通过絮凝剂流量泵的作用控制絮凝剂的进入量，使废油和絮凝剂进入量成规定比例通过进絮凝剂通道吸入搅拌沉降罐中。2) Open the flocculant inlet valve, close the other valves, turn on the flocculant flow pump, and turn off the flocculant flow pump when the flocculant flow rate reaches 3-5V0; control the flocculant flow rate through the function of the flocculant flow pump, so that the waste The amount of oil and flocculant entering is sucked into the stirring and settling tank through the flocculant inlet channel in a specified ratio.
3）打开高温蒸汽进口阀和高温蒸汽出口阀，通入高温蒸汽，并关闭其他阀门，通过控制阀门开度使搅拌沉降罐的温度保持在45-65℃，维持一段时间后，使废润滑油与絮凝剂均匀混合，匀速搅拌1-2h后，停止搅拌，静置沉降12-15h，待油液出现明显分层且液面高度不再变化后，开启水渣阀，将下层液体送入水渣分离器，所产生的水和杂质进行分离，水送入水处理系统，固体杂质则制成印刷油墨或作为铺路沥青加以应用，关闭水渣阀，开启连通阀，将上层油液与絮凝剂混合液送入蒸馏罐；（絮凝剂与废润滑油在搅拌沉降罐进行恒温搅拌。高温水蒸气从搅拌罐下部进入，上部流出，通过间壁换热的方式加热废油。将搅拌器调整到指定的转速并在一定的温度下搅拌一定时间，使絮凝剂与废油进行充分搅拌，待搅拌完全后停止并在搅拌罐中进行静置分离，直至油液出现明显分层且液面高度不再变化。开启絮凝沉降水渣阀，将下层液体送入水渣分离器。）3) Open the high-temperature steam inlet valve and high-temperature steam outlet valve, pass in high-temperature steam, and close other valves, and keep the temperature of the stirring and settling tank at 45-65°C by controlling the opening of the valve. After a period of time, the waste lubricating oil Mix evenly with the flocculant, stir at a constant speed for 1-2 hours, stop stirring, and let it settle for 12-15 hours. The slag separator, the produced water and impurities are separated, the water is sent to the water treatment system, and the solid impurities are made into printing ink or applied as paving asphalt, the water slag valve is closed, and the connecting valve is opened to separate the upper layer of oil and flocculant The mixed liquid is sent to the distillation tank; (the flocculant and the waste lubricating oil are stirred at a constant temperature in the stirring and settling tank. The high-temperature water vapor enters from the lower part of the stirring tank, flows out from the upper part, and heats the waste oil through the heat exchange of the partition wall. Adjust the agitator to the specified and stir at a certain temperature for a certain period of time to fully stir the flocculant and waste oil. After the stirring is complete, stop and separate in the stirring tank until the oil is clearly stratified and the liquid level is no longer Change. Open the flocculation and sedimentation slag valve, and send the lower liquid into the slag separator.)
4）油液与絮凝剂混合液进入蒸馏罐后，开启真空泵阀利用真空泵将蒸馏罐调节到真空度为0.005-0.01Mpa，并在65-80℃下进行混合液体的减压蒸馏；蒸馏出来的絮凝剂蒸汽由蒸馏罐顶部絮凝剂出口的絮凝剂回收阀进入到冷凝管中冷却为液体，进行再循环利用，待蒸馏罐内液面高度不在变化后停止蒸馏；剩余的油液即再生油经过再生油出口流出。4) After the mixture of oil liquid and flocculant enters the distillation tank, open the vacuum pump valve and use the vacuum pump to adjust the vacuum degree of the distillation tank to 0.005-0.01Mpa, and carry out vacuum distillation of the mixed liquid at 65-80°C; The flocculant steam enters the condensation pipe from the flocculant recovery valve at the top flocculant outlet of the distillation tank to be cooled into a liquid for recycling, and the distillation is stopped after the liquid level in the distillation tank does not change; the remaining oil is regenerated oil Flow out through the regenerated oil outlet.
有益效果：与现有技术相比，本发明具有如下的特色及优点：Beneficial effects: compared with the prior art, the present invention has the following characteristics and advantages:
1)本发明集絮凝剂回收与废油再生装置于一体，具有便携、运行成本低、绿色环保等特点，实现了废润滑油的回收再利用。1) The present invention integrates flocculant recovery and waste oil regeneration device, has the characteristics of portability, low operating cost, and environmental protection, and realizes the recovery and reuse of waste lubricating oil.
2)本发明实现了在废油再生的同时进行絮凝剂的实时回收利用，减少了絮凝剂投入成本并提高了装置的运行效率。2) The present invention realizes the real-time recovery and utilization of the flocculant while the waste oil is regenerated, reduces the investment cost of the flocculant and improves the operating efficiency of the device.
3)本发明设计了一种集搅拌与沉降一体的装置搅拌沉降罐，减少了设备投资和占地面积。3) The present invention designs a stirring settling tank which is a device integrating stirring and settling, which reduces equipment investment and floor space.
4)本发明将废油处理所产生的水和杂质进行分离，水送入水处理系统，固体杂质则制成印刷油墨或作为铺路沥青加以应用，提高废物的利用率。4) The present invention separates the water and impurities produced by waste oil treatment, the water is sent to the water treatment system, and the solid impurities are made into printing ink or applied as paving asphalt, so as to improve the utilization rate of waste.
5)本发明通过多个流量阀控制各组分的流量，可以确保各个设备单独运行或者组合运行。5) The present invention controls the flow of each component through multiple flow valves, which can ensure that each device operates independently or in combination.
附图说明Description of drawings
图1是本发明絮凝剂回收式废油再生集成装置；Fig. 1 is the flocculant recovery type waste oil regeneration integrated device of the present invention;
其中：1废油回收装置箱体、2进油阀、3废油流量计、4进絮凝剂阀、5絮凝剂流量泵、6废油过滤网、7搅拌沉降罐、8高温蒸汽进口阀、9高温蒸汽出口阀、10连通阀、11水渣阀、12水渣分离器、13蒸馏罐、14真空泵阀、15真空泵、16絮凝剂回收阀、17冷凝管、18再生油阀；Among them: 1 waste oil recovery device box, 2 oil inlet valve, 3 waste oil flow meter, 4 flocculant valve, 5 flocculant flow pump, 6 waste oil filter, 7 stirring and settling tank, 8 high temperature steam inlet valve, 9 High-temperature steam outlet valve, 10 Connecting valve, 11 Water slag valve, 12 Water slag separator, 13 Distillation tank, 14 Vacuum pump valve, 15 Vacuum pump, 16 Flocculant recovery valve, 17 Condenser pipe, 18 Recovery oil valve;
图2是本发明中使用的搅拌沉降罐的结构图；其中：H1-圆柱结构高度 D1-圆柱结构直径 D2-蒸汽管道直径 D3-水渣管直径 D4-进油管直径 D5-进絮凝剂管直径 D6-出油管直径 θ-沉降罐底部倾斜角。Fig. 2 is the structural diagram of the stirring and settling tank used in the present invention; wherein: H1-cylindrical structure height D1-cylindrical structure diameter D2-steam pipe diameter D3-water slag pipe diameter D4-oil inlet pipe diameter D5-flocculant pipe diameter D6-the diameter of the oil outlet pipe θ-the inclination angle of the bottom of the settling tank.
具体实施方式detailed description
下面通过具体的实施例和附图对本发明进一步说明，应当指出，对于本领域的普通技术人员来说，在不脱离本发明原理的前提下，还可以做出若干变型和改进，这些也应视为属于本发明的保护范围。The present invention will be further described below through specific embodiments and accompanying drawings. It should be pointed out that for those of ordinary skill in the art, some modifications and improvements can also be made without departing from the principle of the present invention. To belong to the protection scope of the present invention.
实施例1：Example 1:
如图1所示，一种絮凝剂回收式废油再生集成装置，该装置主要包括废油回收装置箱体1、在废油回收装置箱体1内部设置的搅拌沉降罐7和通过连通阀10连接的蒸馏罐13，搅拌沉降罐7的上端一侧设有进油阀2和与进油阀2相连的废油流量计3，搅拌沉降罐7的上端另一侧设有进絮凝剂阀4和与进絮凝剂阀4相连的絮凝剂流量泵5，搅拌沉降罐7左侧上端设有高温蒸汽出口阀9和左侧下端设有高温蒸汽进口阀8，搅拌沉降罐7右侧下端设有水渣阀11以及与水渣阀11相连的水渣分离器12；蒸馏罐13上端一侧设有絮凝剂回收阀16和与絮凝剂回收阀16相连的冷凝管17，冷凝管17的另一端与絮凝剂流量泵5相连，蒸馏罐13上端另一侧设有真空泵阀14以及与真空泵阀14相连的真空泵，蒸馏罐13的下侧设有再生油阀18。搅拌沉降罐7的内部设有水蒸汽管道和位于蒸汽管道上方的废油过滤网6。As shown in Figure 1, a flocculant recovery type waste oil regeneration integrated device, the device mainly includes a waste oil recovery device box 1, a stirring settling tank 7 set inside the waste oil recovery device box 1 and a communication valve 10 Connected distillation tank 13, one side of the upper end of the stirring and settling tank 7 is provided with an oil inlet valve 2 and a waste oil flowmeter 3 connected to the oil inlet valve 2, and the other side of the upper end of the stirring and settling tank 7 is provided with a flocculant inlet valve 4 The flocculant flow pump 5 connected with the flocculant inlet valve 4, the upper left end of the stirring and settling tank 7 is provided with a high-temperature steam outlet valve 9 and the lower end of the left is provided with a high-temperature steam inlet valve 8, and the lower end of the stirring and settling tank 7 is provided with a The slag valve 11 and the slag separator 12 connected with the slag valve 11; the upper end of the distillation tank 13 is provided with a flocculant recovery valve 16 and a condensation pipe 17 connected with the flocculant recovery valve 16, and the other end of the condensation pipe 17 It is connected with the flocculant flow pump 5 , the other side of the upper end of the distillation tank 13 is provided with a vacuum pump valve 14 and a vacuum pump connected with the vacuum pump valve 14 , and the lower side of the distillation tank 13 is provided with a regeneration oil valve 18 . The inside of the stirring and settling tank 7 is provided with a steam pipeline and a waste oil filter screen 6 positioned above the steam pipeline.
在本实施例中，搅拌沉降罐7圆柱结构高度H1为1.5m，直径D1为0.5m，水蒸气管道D2直径为0.1m，水渣阀相连的水渣管的直径D3为0.03m，出油管D6直径为0.12m，进油管D4直径为0.05m，进絮凝剂管D5直径为0.1m，倾斜角为3°。废油进油管带有进油阀2与废油流量计3，以方便控制废油进油量。絮凝剂通道带有絮凝剂流量泵5与进絮凝剂阀4，用来控制絮凝剂进入量。搅拌沉降罐7絮凝水渣阀11位于圆锥底部，水蒸气管道进口位于圆柱高度0.3m处，出口位于1.2m处。连通阀相连的出油管即废润滑油出口位于圆柱高度0.45m处。废油回收装置箱体1底部设有两个滚轮。In this embodiment, the height H1 of the cylindrical structure of the stirring and settling tank 7 is 1.5m, the diameter D1 is 0.5m, the diameter of the water vapor pipeline D2 is 0.1m, the diameter D3 of the water slag pipe connected to the water slag valve is 0.03m, and the oil outlet pipe The diameter of D6 is 0.12m, the diameter of oil inlet pipe D4 is 0.05m, the diameter of flocculant inlet pipe D5 is 0.1m, and the inclination angle is 3°. The waste oil inlet pipe is provided with an oil inlet valve 2 and a waste oil flow meter 3 to facilitate the control of the amount of waste oil inlet. The flocculant channel is equipped with a flocculant flow pump 5 and a flocculant inlet valve 4, which are used to control the amount of flocculant entering. The flocculation slag valve 11 of the stirring settling tank 7 is located at the bottom of the cone, the inlet of the water vapor pipeline is located at a height of 0.3m of the cylinder, and the outlet is located at 1.2m. The oil outlet pipe connected to the communication valve, that is, the waste lubricating oil outlet, is located at a cylinder height of 0.45m. Two rollers are arranged at the bottom of the waste oil recovery device casing 1 .
一种絮凝剂回收式废油再生集成装置在回收钢铁行业中废油方面的应用。The application of a flocculant recovery type waste oil regeneration integrated device in the recovery of waste oil in the iron and steel industry.
所述的应用，具体为一种絮凝剂回收式废油再生方法，该方法包括如下步骤：本实施例采用南钢220#中负荷工业齿轮废润滑油（下称废齿轮油），絮凝剂采用正丁醇。The above-mentioned application is specifically a flocculant recovery type waste oil regeneration method, which includes the following steps: In this embodiment, Nangang 220# medium-duty industrial gear waste lubricating oil (hereinafter referred to as waste gear oil) is used, and the flocculant adopts n-butanol.
1）打开进油阀2、连通阀10和真空泵阀14，关闭其他阀门，由真空泵15提供动力，采用将经过静止沉降后的废齿轮油上层油液通过废油流量计3，将体积为0.25m3的废齿轮油送入搅拌沉降罐7中，并在搅拌沉降罐7上部通过废油过滤网6时完成初步过滤；1) Open the oil inlet valve 2, the communication valve 10 and the vacuum pump valve 14, close other valves, and the power is provided by the vacuum pump 15. The upper layer of the waste gear oil after static settlement is passed through the waste oil flow meter 3, and the volume isThe waste gear oil of 0.25m3 is sent in the stirring and settling tank 7, and the preliminary filtration is completed when the upper part of the stirring and settling tank 7 passes through the waste oil filter screen 6;
2）打开进絮凝剂阀4，关闭其余阀门，打开絮凝剂流量泵5，当絮凝剂进量达到0.75m3时关闭絮凝剂流量泵5；2) Open the flocculant inlet valve 4, close the other valves, turn on the flocculant flow pump 5, and turn off the flocculant flow pump5 when the flocculant intake reaches 0.75m3;
3）打开高温蒸汽进口阀8和高温蒸汽出口阀9，通入高温蒸汽，并关闭其他阀门，通过控制阀门开度使搅拌沉降罐7的温度保持在45℃，维持一段时间后，使废齿轮油与正丁醇均匀混合，匀速搅拌2h后，停止搅拌，静置沉降12h，待油液出现明显分层且液面高度不再变化后，开启水渣阀11，将下层液体送入水渣分离器12，所产生的水和杂质进行分离，水送入水处理系统，固体杂质则制成印刷油墨或作为铺路沥青加以应用，关闭水渣阀11，开启连通阀10，将上层油液与絮凝剂混合液送入蒸馏罐13；3) Open the high-temperature steam inlet valve 8 and the high-temperature steam outlet valve 9, pass in high-temperature steam, and close other valves, and keep the temperature of the stirring and settling tank 7 at 45°C by controlling the valve opening. After a period of time, the waste gear Mix the oil and n-butanol evenly, stir at a constant speed for 2 hours, stop stirring, and let it settle for 12 hours. After the oil liquid has obvious stratification and the liquid level no longer changes, open the slag valve 11 to send the lower liquid into the slag Separator 12, the generated water and impurities are separated, the water is sent to the water treatment system, and the solid impurities are made into printing ink or used as paving asphalt, close the water slag valve 11, open the communication valve 10, and separate the upper oil and The flocculant mixed solution is sent into the distillation tank 13;
4）油液与絮凝剂混合液进入蒸馏罐13后，开启真空泵阀14利用真空泵15将蒸馏罐13调节到真空度为0.005Mpa，并在65℃下进行混合液体的减压蒸馏；蒸馏出来的絮凝剂蒸汽由蒸馏罐13顶部絮凝剂出口的絮凝剂回收阀16进入到冷凝管17中冷却为液体，进行再循环利用，待蒸馏罐13内液面高度不在变化后停止蒸馏；剩余的再生油经过再生油出口18流出。4) After the mixture of oil and flocculant enters the distillation tank 13, turn on the vacuum pump valve 14 and use the vacuum pump 15 to adjust the vacuum degree of the distillation tank 13 to 0.005Mpa, and carry out vacuum distillation of the mixed liquid at 65°C; The flocculant vapor enters the condensation pipe 17 from the flocculant recovery valve 16 at the flocculant outlet on the top of the retort 13 to be cooled into a liquid for recycling, and the distillation is stopped after the liquid level in the retort 13 does not change; the remaining regeneration Oil exits through regenerated oil outlet 18 .
实施例2：Example 2:
如图1所示，一种絮凝剂回收式废油再生集成装置，该装置主要包括废油回收装置箱体1、在废油回收装置箱体1内部设置的搅拌沉降罐7和通过连通阀10连接的蒸馏罐13，搅拌沉降罐7的上端一侧设有进油阀2和与进油阀2相连的废油流量计3，搅拌沉降罐7的上端另一侧设有进絮凝剂阀4和与进絮凝剂阀4相连的絮凝剂流量泵5，搅拌沉降罐7左侧上端设有高温蒸汽出口阀9和左侧下端设有高温蒸汽进口阀8，搅拌沉降罐7右侧下端设有水渣阀11以及与水渣阀11相连的水渣分离器12；蒸馏罐13上端一侧设有絮凝剂回收阀16和与絮凝剂回收阀16相连的冷凝管17，冷凝管17的另一端与絮凝剂流量泵5相连，蒸馏罐13上端另一侧设有真空泵阀14以及与真空泵阀14相连的真空泵，蒸馏罐13的下侧设有再生油阀18。搅拌沉降罐7的内部设有水蒸汽管道和位于蒸汽管道上方的废油过滤网6。As shown in Figure 1, a flocculant recovery type waste oil regeneration integrated device, the device mainly includes a waste oil recovery device box 1, a stirring settling tank 7 set inside the waste oil recovery device box 1 and a communication valve 10 Connected distillation tank 13, one side of the upper end of the stirring and settling tank 7 is provided with an oil inlet valve 2 and a waste oil flowmeter 3 connected to the oil inlet valve 2, and the other side of the upper end of the stirring and settling tank 7 is provided with a flocculant inlet valve 4 The flocculant flow pump 5 connected with the flocculant inlet valve 4, the upper left end of the stirring and settling tank 7 is provided with a high-temperature steam outlet valve 9 and the lower end of the left is provided with a high-temperature steam inlet valve 8, and the lower end of the stirring and settling tank 7 is provided with a The slag valve 11 and the slag separator 12 connected with the slag valve 11; the upper end of the distillation tank 13 is provided with a flocculant recovery valve 16 and a condensation pipe 17 connected with the flocculant recovery valve 16, and the other end of the condensation pipe 17 It is connected with the flocculant flow pump 5 , the other side of the upper end of the distillation tank 13 is provided with a vacuum pump valve 14 and a vacuum pump connected with the vacuum pump valve 14 , and the lower side of the distillation tank 13 is provided with a regeneration oil valve 18 . The inside of the stirring and settling tank 7 is provided with a steam pipeline and a waste oil filter screen 6 positioned above the steam pipeline.
在本实施例中，搅拌沉降罐7圆柱结构高度H1为2.0m，直径D1为0.6m，水蒸气管道直径D2为0.15m，水渣阀相连的水渣管的直径D3为0.02m，出油管D6直径为0.15m，进油管D4直径为0.08m，进絮凝剂管直径D5为0.1m，倾斜角为4°。废油进油管带有进油阀2与废油流量计3，以方便控制废油进油量。絮凝剂通道带有絮凝剂流量泵5与进絮凝剂阀4，用来控制絮凝剂进入量。搅拌沉降罐7絮凝水渣阀11位于圆锥底部，水蒸气管道进口位于圆柱高度0.4m处，出口位于1.6m处。连通阀相连的出油管即废润滑油出口位于圆柱高度0.6m处。废油回收装置箱体1底部设有两个滚轮。In this embodiment, the height H1 of the cylindrical structure of the stirring and settling tank 7 is 2.0m, the diameter D1 is 0.6m, the diameter D2 of the water vapor pipeline is 0.15m, the diameter D3 of the water slag pipe connected with the water slag valve is 0.02m, and the oil outlet pipe The diameter of D6 is 0.15m, the diameter of oil inlet pipe D4 is 0.08m, the diameter of flocculant inlet pipe D5 is 0.1m, and the inclination angle is 4°. The waste oil inlet pipe is provided with an oil inlet valve 2 and a waste oil flow meter 3 to facilitate the control of the amount of waste oil inlet. The flocculant channel is equipped with a flocculant flow pump 5 and a flocculant inlet valve 4, which are used to control the amount of flocculant entering. The flocculation slag valve 11 of the stirring settling tank 7 is located at the bottom of the cone, the inlet of the water vapor pipeline is located at the height of the cylinder at 0.4m, and the outlet is located at 1.6m. The oil outlet pipe connected to the communication valve, that is, the outlet of waste lubricating oil, is located at the height of the cylinder at 0.6m. Two rollers are arranged at the bottom of the waste oil recovery device casing 1 .
一种絮凝剂回收式废油再生集成装置在回收钢铁行业中废油方面的应用。The application of a flocculant recovery type waste oil regeneration integrated device in the recovery of waste oil in the iron and steel industry.
所述的应用，具体为一种絮凝剂回收式废油再生方法，该方法包括如下步骤：本实施例采用南钢废液压油，絮凝剂采用甲基乙基酮。The application described above is specifically a flocculant-recovery waste oil regeneration method, which includes the following steps: In this embodiment, waste hydraulic oil from Nanjing Iron and Steel Co., Ltd. is used, and methyl ethyl ketone is used as a flocculant.
1）打开进油阀2、连通阀10和真空泵阀14，关闭其他阀门，由真空泵15提供动力，采用将经过静止沉降后的废液压油上层油液通过废油流量计3，将体积为0.35m3的废液压油送入搅拌沉降罐7中，并在搅拌沉降罐7上部通过废油过滤网6时完成初步过滤；1) Open the oil inlet valve 2, the communication valve 10 and the vacuum pump valve 14, close other valves, and the power is provided by the vacuum pump 15. The upper layer of the waste hydraulic oil after static settlement is passed through the waste oil flowmeter 3, and the volume is The waste hydraulic oil of0.35m3 is sent into the stirring and settling tank 7, and the preliminary filtration is completed when the upper part of the stirring and settling tank 7 passes through the waste oil filter screen 6;
2）打开进絮凝剂阀4，关闭其余阀门，打开絮凝剂流量泵5，当絮凝剂进量达到1.0m3时关闭絮凝剂流量泵5；2) Open the flocculant inlet valve 4, close the other valves, turn on the flocculant flow pump 5, and turn off the flocculant flow pump5 when the flocculant intake reaches 1.0m3;
3）打开高温蒸汽进口阀8和高温蒸汽出口阀9，通入高温蒸汽，并关闭其他阀门，通过控制阀门开度使搅拌沉降罐7的温度保持在60℃，维持一段时间后，使废液压油与正丁醇均匀混合，匀速搅拌3h后，停止搅拌，静置沉降12h，待油液出现明显分层且液面高度不再变化后，开启水渣阀11，将下层液体送入水渣分离器12，所产生的水和杂质进行分离，水送入水处理系统，固体杂质则制成印刷油墨或作为铺路沥青加以应用，关闭水渣阀11，开启连通阀10，将上层油液与絮凝剂混合液送入蒸馏罐13；3) Open the high-temperature steam inlet valve 8 and the high-temperature steam outlet valve 9, pass in high-temperature steam, and close other valves, and keep the temperature of the stirring and settling tank 7 at 60°C by controlling the opening of the valve. After a period of time, the waste hydraulic pressure Mix the oil and n-butanol evenly, stir at a constant speed for 3 hours, stop stirring, and let it settle for 12 hours. After the oil liquid has obvious stratification and the liquid level no longer changes, open the slag valve 11 to send the lower liquid into the slag Separator 12, the generated water and impurities are separated, the water is sent to the water treatment system, and the solid impurities are made into printing ink or used as paving asphalt, close the water slag valve 11, open the communication valve 10, and separate the upper oil and The flocculant mixed solution is sent into the distillation tank 13;
4）油液与絮凝剂混合液进入蒸馏罐13后，开启真空泵阀14利用真空泵15将蒸馏罐13调节到真空度为0.01Mpa，并在70℃下进行混合液体的减压蒸馏；蒸馏出来的絮凝剂蒸汽由蒸馏罐13顶部絮凝剂出口的絮凝剂回收阀16进入到冷凝管17中冷却为液体，进行再循环利用，待蒸馏罐13内液面高度不在变化后停止蒸馏；剩余的再生油经过再生油出口18流出。4) After the mixture of oil and flocculant enters the distillation tank 13, turn on the vacuum pump valve 14 and use the vacuum pump 15 to adjust the vacuum degree of the distillation tank 13 to 0.01Mpa, and carry out vacuum distillation of the mixed liquid at 70°C; The flocculant vapor enters the condensation pipe 17 from the flocculant recovery valve 16 at the flocculant outlet on the top of the retort 13 to be cooled into a liquid for recycling, and the distillation is stopped after the liquid level in the retort 13 does not change; the remaining regeneration Oil exits through regenerated oil outlet 18 .
实施例3：Example 3:
与实施例1基本一样，所不同的在于，在本实施例中，搅拌沉降罐7圆柱结构高度H1为1.8m，直径D1为0.4m，水蒸气管道直径为D2为0.2m，水渣阀相连的水渣管的直径D3为0.05m，进油阀相连的进油管的直径D4为0.1m，进絮凝剂阀相连的进絮凝剂管的直径D5为0.1m，出油管的直径D6为0.1m，倾斜角为5°。废油进油管带有进油阀2与废油流量计3，以方便控制废油进油量。絮凝剂通道带有絮凝剂流量泵5与进絮凝剂阀4，用来控制絮凝剂进入量。搅拌沉降罐7絮凝水渣阀11位于圆锥底部，水蒸气管道进口位于圆柱高度0.36m处，出口位于1.44m处。连通阀相连的出油管即废润滑油出口位于圆柱高度0.54m处。废油回收装置箱体1底部设有两个滚轮。Basically the same as Example 1, the difference is that in this example, the height H1 of the cylindrical structure of the agitated settling tank 7 is 1.8m, the diameter D1 is 0.4m, the diameter of the water vapor pipeline is D2 is 0.2m, and the water slag valve is connected The diameter D3 of the slag pipe is 0.05m, the diameter D4 of the oil inlet pipe connected to the oil inlet valve is 0.1m, the diameter D5 of the flocculant inlet pipe connected to the flocculant inlet valve is 0.1m, and the diameter D6 of the oil outlet pipe is 0.1m , with an inclination angle of 5°. The waste oil inlet pipe is provided with an oil inlet valve 2 and a waste oil flow meter 3 to facilitate the control of the amount of waste oil inlet. The flocculant channel is equipped with a flocculant flow pump 5 and a flocculant inlet valve 4, which are used to control the amount of flocculant entering. The flocculation slag valve 11 of the agitating settling tank 7 is located at the bottom of the cone, the inlet of the water vapor pipeline is located at a cylinder height of 0.36m, and the outlet is located at 1.44m. The oil outlet pipe connected to the communication valve, that is, the outlet of the waste lubricating oil, is located at a cylinder height of 0.54m. Two rollers are arranged at the bottom of the waste oil recovery device casing 1 .
一种絮凝剂回收式废油再生集成装置在回收钢铁行业中废油方面的应用。The application of a flocculant recovery type waste oil regeneration integrated device in the recovery of waste oil in the iron and steel industry.
所述的应用，具体为一种絮凝剂回收式废油再生方法，该方法包括如下步骤：本实施例采用南钢220#中负荷工业齿轮废润滑油（下称废齿轮油），絮凝剂采用正丁醇。The above-mentioned application is specifically a flocculant recovery type waste oil regeneration method, which includes the following steps: In this embodiment, Nangang 220# medium-duty industrial gear waste lubricating oil (hereinafter referred to as waste gear oil) is used, and the flocculant adopts n-butanol.
1）打开进油阀2、连通阀10和真空泵阀14，关闭其他阀门，由真空泵15提供动力，采用将经过静止沉降后的废齿轮油上层油液通过废油流量计3，将体积为0.25m3的废齿轮油送入搅拌沉降罐7中，并在搅拌沉降罐7上部通过废油过滤网6时完成初步过滤；1) Open the oil inlet valve 2, the communication valve 10 and the vacuum pump valve 14, close other valves, and the power is provided by the vacuum pump 15. The upper layer of the waste gear oil after static settlement is passed through the waste oil flow meter 3, and the volume isThe waste gear oil of 0.25m3 is sent in the stirring and settling tank 7, and the preliminary filtration is completed when the upper part of the stirring and settling tank 7 passes through the waste oil filter screen 6;
2）打开进絮凝剂阀4，关闭其余阀门，打开絮凝剂流量泵5，当絮凝剂进量达到0.75m3时关闭絮凝剂流量泵5；2) Open the flocculant inlet valve 4, close the other valves, turn on the flocculant flow pump 5, and turn off the flocculant flow pump5 when the flocculant intake reaches 0.75m3;
3）打开高温蒸汽进口阀8和高温蒸汽出口阀9，通入高温蒸汽，并关闭其他阀门，通过控制阀门开度使搅拌沉降罐7的温度保持在65℃，维持一段时间后，使废齿轮油与正丁醇均匀混合，匀速搅拌2h后，停止搅拌，静置沉降12h，待油液出现明显分层且液面高度不再变化后，开启水渣阀11，将下层液体送入水渣分离器12，所产生的水和杂质进行分离，水送入水处理系统，固体杂质则制成印刷油墨或作为铺路沥青加以应用，关闭水渣阀11，开启连通阀10，将上层油液与絮凝剂混合液送入蒸馏罐13；3) Open the high-temperature steam inlet valve 8 and the high-temperature steam outlet valve 9, pass in high-temperature steam, and close other valves, and keep the temperature of the stirring and settling tank 7 at 65°C by controlling the valve opening. After a period of time, the waste gear Mix the oil and n-butanol evenly, stir at a constant speed for 2 hours, stop stirring, and let it settle for 12 hours. After the oil liquid has obvious stratification and the liquid level no longer changes, open the slag valve 11 to send the lower liquid into the slag Separator 12, the generated water and impurities are separated, the water is sent to the water treatment system, and the solid impurities are made into printing ink or used as paving asphalt, close the water slag valve 11, open the communication valve 10, and separate the upper oil and The flocculant mixed solution is sent into the distillation tank 13;
4）油液与絮凝剂混合液进入蒸馏罐13后，开启真空泵阀14利用真空泵15将蒸馏罐13调节到真空度为0.008Mpa，并在80℃下进行混合液体的减压蒸馏；蒸馏出来的絮凝剂蒸汽由蒸馏罐13顶部絮凝剂出口的絮凝剂回收阀16进入到冷凝管17中冷却为液体，进行再循环利用，待蒸馏罐13内液面高度不在变化后停止蒸馏；剩余的再生油经过再生油出口18流出。4) After the mixture of oil and flocculant enters the distillation tank 13, turn on the vacuum pump valve 14 and use the vacuum pump 15 to adjust the vacuum degree of the distillation tank 13 to 0.008Mpa, and carry out vacuum distillation of the mixed liquid at 80°C; The flocculant vapor enters the condensation pipe 17 from the flocculant recovery valve 16 at the flocculant outlet on the top of the retort 13 to be cooled into a liquid for recycling, and the distillation is stopped after the liquid level in the retort 13 does not change; the remaining regeneration Oil exits through regenerated oil outlet 18 .
上述仅为本发明优选的实施例，并不限制于本发明。对于所属领域的技术人员来说，在上述说明的基础上还可以做出其他不同形式的变化或变动。这里无需也无法对所有的实施例来举例说明。而由此方案所引伸出的显而易见的变化或变动仍处于本发明的保护范围之内。The above are only preferred embodiments of the present invention, and do not limit the present invention. For those skilled in the art, other changes or changes in different forms can be made on the basis of the above description. It is not necessary and not possible to illustrate all embodiments here. However, the obvious changes or changes derived from this solution are still within the protection scope of the present invention.
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510093916.0ACN104726192B (en) | 2015-03-03 | 2015-03-03 | A kind of flocculant recovery type waste oil regeneration integrating device and its application |
| Application Number | Priority Date | Filing Date | Title |
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| CN201510093916.0ACN104726192B (en) | 2015-03-03 | 2015-03-03 | A kind of flocculant recovery type waste oil regeneration integrating device and its application |
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| CN104726192A CN104726192A (en) | 2015-06-24 |
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| CN201510093916.0AActiveCN104726192B (en) | 2015-03-03 | 2015-03-03 | A kind of flocculant recovery type waste oil regeneration integrating device and its application |
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| CN104726192B (en) | A kind of flocculant recovery type waste oil regeneration integrating device and its application | |
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