CN210394006U - Contain quick oil-water separation's of miscellaneous soap-containing emulsified oil device - Google Patents
Contain quick oil-water separation's of miscellaneous soap-containing emulsified oil device Download PDFInfo
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- CN210394006U CN210394006U CN201921102046.9U CN201921102046U CN210394006U CN 210394006 U CN210394006 U CN 210394006U CN 201921102046 U CN201921102046 U CN 201921102046U CN 210394006 U CN210394006 U CN 210394006U
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Abstract
The utility model provides a contain quick oil-water separation's of miscellaneous soap-containing emulsified oil device. The device is characterized in that a mixed oil-water storage tank and a flocculating agent storage tank in the device are communicated with a water distribution tank through pipelines, a stirring motor and a speed reducer are mounted at the top of the water distribution tank, the bottom of the water distribution tank is communicated with an observation window, a sewage treatment station, a three-position electromagnetic valve, a centrifugal pump and a collecting tank through pipelines, the collecting tank is communicated with a reduced-pressure vacuum dehydration mechanism through a pipeline, the reduced-pressure vacuum dehydration mechanism is communicated with a filtering mechanism through a pipeline, and the output end of the filtering mechanism is communicated with a next procedure through a. The device adopts polyacrylamide to carry out the flash separation with oil, water, sediment for the flocculating agent, stirring in the water knockout drum, handles respectively residue, water and grease clarified liquid after the separation, and the device structural design is reasonable, and convenience, facilitate promotion and application very use and maintenance.
Description
Technical Field
The utility model relates to chemical industry equipment and waste water treatment field, in particular to contain quick oil-water separation's of miscellaneous soap-containing emulsified oil device.
Background
The oil-water separation is always an important content in the field of oil purification, and the oil-water separation technologies such as sedimentation, adsorption, centrifugation, vacuum separation, cyclone separation and the like which are adopted in the past can well separate non-milky water in oil, so that the oil-water separation method and the oil-water separation device are technical means and methods which are generally adopted in the field of oil purification. For the problem of emulsion oil dehydration, the prior known technical method is to respectively carry out the demulsification process and the dehydration process by adopting different technical methods, which also causes the problems of increased process units, low treatment efficiency, high production cost and the like in the industrialized demulsification and dehydration process. At present, the emulsified oil containing water and miscellaneous soaps, which is discharged in most chemical enterprises at present, is very difficult to rapidly divide water, and the main problems are mainly shown as follows: 1. the emulsified oil needs to be kept warm for a long time in a water separation tank, and the standing time is long, so that energy and time are wasted, a large amount of water is still contained after water separation, and great trouble is still brought to further treatment; 2. if a centrifuge is used for separating oil, water and impurities, the impurities can cause difficulty in slag discharge of the centrifuge, and the centrifuge needs to be frequently disassembled for slag removal. Rapid wear and damage to the centrifuge can also result. The appearance of novel high-effect oil-water separation nano material makes it possible to carry out single treatment to realize emulsion breaking and dehydration of the emulsion liquid, and through reasonable technical means, not only can the emulsion liquid be dehydrated and purified, but also the use of a large amount of chemical demulsifiers can be avoided, thereby reducing pollution emission and simultaneously reducing the treatment process unit and the treatment cost. However, the practical application of the high performance oil-water separation material in the field of demulsification and dehydration is still very rare so far, and particularly, the attempts of performing demulsification and dehydration only by using the oil-water separation material are few, because a comprehensive solution method is lacked, so that the high performance oil-water separation material can simultaneously solve the problems of demulsification and dehydration of emulsion.
Patent application No. 201710325577.3 discloses a method for purifying high-emulsified-oil-content sewage, which is mainly technically characterized in that: adding a demulsifier into the high-emulsified-oil-content sewage, adding 1.0-5.0 mg of the demulsifier into each liter of the high-emulsified-oil-content sewage, then inputting the high-emulsified-oil-content sewage into a pipeline mixer, fully mixing, then carrying out high-speed dispersion treatment on the high-emulsified-oil-content sewage by using a high-speed dispersion pump 5, inputting the treated liquid into an oil-water separator, after reaction, discharging the floating oil regularly or discharging the floating oil through an oil receiving port after monitoring by an oil-water interface detector, and discharging the purified water through a water outlet, thus purifying the high-emulsified-oil-content sewage.
Patent No. 201110255565.0 discloses a petrochemical emulsification process water oil removal method, which is mainly technically characterized in that: after the demulsifier is added into the emulsified process water, the emulsified process water sequentially passes through the demulsification sedimentation unit, the coarse granulation filtering unit and the interception oil removal unit, so that oil and water are separated, and the oil and the water are respectively recycled through pipelines.
In the above patent documents, all methods for separating oil from water in emulsified oil are methods of separating oil from water by adding a demulsifier to oil and water, and no technical teaching is given for separating oil from water by other methods.
Disclosure of Invention
An object of the utility model is to provide a contain quick oil-water separator of miscellaneous soap-containing emulsified oil.
The utility model discloses an utilize Polyacrylamide (PAM) to be the flocculating agent, go into the knockout drum with Polyacrylamide (PAM) liquid medicine and water oil mixed liquid through the different pipeline pump for the measuring pump, the flowmeter that uses in the pipeline is used for control and measures the addition of liquid medicine and water oil mixed liquid, stir the oil that makes in the mixed liquid by agitator motor drive (mixing) shaft and blade to mixed liquid, water, sediment flash segregation, residue and the waste water discharge after the separation handles in the sewage treatment station, the grease clarified liquid that contains trace water and sediment after the separation is gone into the holding treatment in the collection tank through the centrifugal pump, grease clarified liquid in the collection tank heats through decompression vacuum dehydration mechanism, the vacuum distillation, obtain the qualified finished product grease that does not contain sediment and water through filter mechanism at last. The electromagnetic valve used in the whole system is used for controlling the liquid in the pipeline to enter or stop, and the liquid level probe and the liquid level meter are used for monitoring the liquid level of the mixed liquid in the water distribution tank.
In order to achieve the above purpose, the technical scheme of the utility model is that:
a contain quick oil-water separator of miscellaneous soap-containing emulsified oil, includes: the device comprises a mixed oil-water storage tank, a first electromagnetic valve, a first metering pump, a first flowmeter, a flocculating agent storage tank, a second electromagnetic valve, a second metering pump, a second flowmeter, a stirring motor, a speed reducer, a stirring shaft, a water diversion tank, blades, a liquid level meter, an observation window, a third electromagnetic valve, a fourth electromagnetic valve, a first centrifugal pump, a collection tank, a fifth electromagnetic valve, a second centrifugal pump, a pressure reduction vacuum dehydration mechanism, a sixth electromagnetic valve, a filtering mechanism, a liquid level probe and a control console, wherein the mixed oil-water storage tank in the device is communicated with the input end of the first metering pump through a pipeline, the first electromagnetic valve is arranged on a connecting pipeline, the output end of the first metering pump is communicated with the water diversion tank through a pipeline, the first flowmeter is arranged on the connecting pipeline, the flocculating agent storage tank is communicated with the input end of the second metering pump through a pipeline, the second electromagnetic valve is, the top mounting bracket of the water diversion tank is provided with a stirring motor, the output shaft of the stirring motor is provided with a speed reducer, the output shaft of the speed reducer is connected with a stirring shaft provided with blades, the pipeline at the bottom of the water diversion tank is provided with an observation window, the pipeline is communicated with a sewage treatment station, the connecting pipeline is provided with a third electromagnetic valve, the connecting pipeline is communicated with the input end of a first centrifugal pump through a three-way pipe, the connecting pipeline is provided with a fourth electromagnetic valve, the output end of the first centrifugal pump is communicated with the collecting tank through a pipeline, the lower part of the collecting tank is communicated with a second centrifugal pump through a pipeline, the connecting pipeline is provided with a fifth electromagnetic valve, the output end of the second centrifugal pump is communicated with the input end of a reduced-pressure vacuum dehydration mechanism through a pipeline, the output end of the reduced-pressure vacuum dehydration mechanism is communicated with the input.
A liquid level probe is arranged at the upper part of a water distribution tank in the device, a liquid level meter is arranged at one side of the water distribution tank, and the liquid level meter is communicated with the inner space of the water distribution tank.
A first metering pump, a second metering pump, a first centrifugal pump, a second centrifugal pump, a stirring motor, a first flow meter, a second flow meter, a liquid level probe, a first electromagnetic valve, a second electromagnetic valve, a third electromagnetic valve, a fourth electromagnetic valve, a fifth electromagnetic valve and a sixth electromagnetic valve in the device are respectively connected with a control console through data lines.
The device for quickly separating oil and water from the miscellaneous soap-containing emulsified oil operates according to the following steps:
1. inputting process parameters: before use, technological parameters of a first metering pump, a second metering pump, a stirring motor, a first flowmeter, a second flowmeter, a first centrifugal pump, a second centrifugal pump, a first electromagnetic valve, a second electromagnetic valve, a third electromagnetic valve, a fourth electromagnetic valve, a fifth electromagnetic valve, a sixth electromagnetic valve and a liquid level probe are input into a control console;
2. conveying mixed oil water: the control console sends an instruction to start a first electromagnetic valve and a first metering pump, mixed oil and water in a mixed oil water tank are pumped into the water diversion tank through a pipeline, a first flowmeter arranged on the pipeline is used for controlling and monitoring the adding amount of the mixed oil and water, meanwhile, a liquid level meter is used for observing the liquid level condition in the water diversion tank, when a liquid level probe detects that the mixed oil and water in the water diversion tank reaches the process requirement, the liquid level probe sends a signal to the control console, the control console sends an instruction to close the first electromagnetic valve and the first metering pump, the injection of the mixed oil and water into the water diversion tank is stopped, the mixed oil and water in the water diversion tank is heated at the same time, and the heating temperature is;
3. conveying of liquid medicine: when the heating in the water diversion tank meets the process requirements, the console sends out an instruction, a second electromagnetic valve and a second metering pump are started, Polyacrylamide (PAM) aqueous solution with the mass percentage concentration of 1% in the flocculating agent storage tank is pumped into the water diversion tank through a pipeline by the second metering pump according to the 1/10 amount of the added amount of the mixed oil and water, namely the weight ratio of the added amount of the liquid medicine to the added amount of the mixed oil and water is 1:10, and a second flowmeter arranged on a connecting pipeline is used for controlling and monitoring the added amount of the liquid medicine;
4. stirring the mixed solution: after the liquid medicine is added, the console sends an instruction to close the second electromagnetic valve and the second metering pump, the liquid medicine injection into the water distribution tank is stopped, meanwhile, a stirring motor arranged on the mounting frame is driven to work, the stirring motor drives a speed reducer to rotate, the speed reducer drives a stirring shaft and blades connected with the speed reducer to stir and separate the mixed liquid in the water distribution tank, the stirring time is 3-10 minutes, and the mixed liquid is kept stand for 30-120 minutes after the stirring is finished, so that the water, the slag and the grease clear liquid at the lower layer of the water distribution tank are separated;
5. discharge of sewage and residue: after separation is completed, the console sends an instruction to open a third electromagnetic valve arranged on a pipeline connected with the sewage treatment station at the bottom of the water diversion tank, water and residues generated in the lower layer of the water diversion tank are discharged into the sewage treatment station through the pipeline for treatment, the discharge condition of the water and the residues is monitored through an observation window, when the water and the residues are observed to be discharged, the console sends an instruction to close the third electromagnetic valve, simultaneously opens a fourth electromagnetic valve and a first centrifugal pump, and pumps grease clarified liquid into a collection tank for later use;
6. treating the grease clarified liquid: the console sends an instruction to open a fifth electromagnetic valve and a second centrifugal pump which are arranged on the connecting pipeline, the grease clarified liquid is input into the decompression vacuum dehydration mechanism for further dehydration treatment, then the console sends an instruction to open a sixth electromagnetic valve, the grease clarified liquid treated by the decompression vacuum dehydration mechanism is conveyed into the filtering mechanism for filtering treatment, the trace residue contained in the grease clarified liquid is filtered, and the qualified finished grease without residue and water is obtained after the filtering treatment.
The metering pump, the centrifugal pump, the flowmeter, the stirring motor, the liquid level probe, the electromagnetic valve, the decompression vacuum dehydration mechanism and the filtering mechanism used in the device are all mature and universal equipment or products in the field, wherein the metering pump, the centrifugal pump, the flowmeter, the liquid level probe, the stirring motor and the electromagnetic valve are all universal in the field in the prior art and commercially available products, the use of the corresponding metering pump, the centrifugal pump, the flowmeter, the liquid level probe, the stirring motor and the electromagnetic valve can be determined according to different process conditions, and the types of the metering pump, the centrifugal pump, the flowmeter, the liquid level probe, the electromagnetic valve and the corresponding stirring motor in the field in the prior art can be selected according to different application processes. The connection mode of the metering pump, the centrifugal pump, the flowmeter, the electromagnetic valve and the liquid level probe can be connected according to the instructions provided on the factory specifications of a product manufacturer. The object to be protected in the present application is the combination and corresponding connection relationship of various components, and the model number and connection mode of each component are not strictly limited.
Compared with the prior art, the utility model discloses an actively the effect does:
1. the method adopts Polyacrylamide (PAM) as a flocculating agent, oil, water and slag are quickly separated in a water separation tank by stirring, and separated residues, water and grease clarified liquid are respectively treated;
2. the method can reduce the time required by the emulsified oil in the water separation tank for heat preservation and standing, and simultaneously reduce the consumption and waste of energy sources;
3. the device can respectively treat the separated residue, water and grease clarified liquid through different equipment, so that the grease contained in the emulsified oil can be recycled;
4. the device can realize quick separation and high-efficiency separation when separating emulsified oil, and has low cost of separating the emulsified oil and good separation effect of the emulsified oil;
5. the device has reasonable structural design, convenient use and maintenance, and convenient popularization and application.
Drawings
FIG. 1 is a schematic structural diagram of a device for rapidly separating oil from water, containing miscellaneous emulsified oil containing soap;
FIG. 2 is a connection diagram of control parts of a rapid oil-water separation device for emulsified oil containing impurities and soaps.
In the figure: 1. the device comprises a mixed oil-water storage tank, 2, a first electromagnetic valve, 3, a first metering pump, 4, a first flowmeter, 5, a flocculating agent storage tank, 6, a second electromagnetic valve, 7, a second metering pump, 8, a second flowmeter, 9, a mounting rack, 10, a stirring motor, 11, a speed reducer, 12, a stirring shaft, 13, a water diversion tank, 14, blades, 15, a liquid level meter, 16, an observation window, 17, a sewage treatment station, 18, a third electromagnetic valve, 19, a fourth electromagnetic valve, 20, a first centrifugal pump, 21, a collection tank, 22, a fifth electromagnetic valve, 23, a second centrifugal pump, 24, a decompression vacuum dehydration mechanism, 25, a sixth electromagnetic valve, 26, a filtering mechanism, 27, a liquid level probe, 28 and a control console.
Detailed Description
The technical solution of the present invention will be further clearly and completely described with reference to the accompanying drawings and examples.
Referring to attached drawings 1-2, a mixed oil-water storage tank 1 in the device is communicated with the input end of a first metering pump 3 through a pipeline, a first electromagnetic valve 2 is arranged on the connecting pipeline, the output end of the first metering pump 3 is communicated with a water diversion tank 13 through a pipeline, a first flow meter 4 is arranged on the connecting pipeline, a flocculating agent storage tank 5 is communicated with the input end of a second metering pump 7 through a pipeline, a second electromagnetic valve 6 is arranged on the connecting pipeline, the output end of the second metering pump 7 is communicated with the water diversion tank 13 through a pipeline, a stirring motor 10 is arranged on a mounting frame 9 at the top of the water diversion tank 13, a speed reducer 11 is arranged on an output shaft of the stirring motor 10, an output shaft of the speed reducer 11 is connected with a stirring shaft 12 provided with blades 14, a water diversion observation window 16 is arranged on the pipeline at the bottom of the tank 13, the pipeline is communicated with a sewage treatment station, the four-solenoid valve 19 is arranged on the connecting pipeline, the output end of the first centrifugal pump 20 is communicated with the collecting tank 21 through a pipeline, the lower part of the collecting tank 21 is communicated with the input end of the second centrifugal pump 23 through a pipeline, the five-solenoid valve 22 is arranged on the connecting pipeline, the output end of the second centrifugal pump 23 is communicated with the input end of the pressure-reducing vacuum dewatering mechanism 24 through a pipeline, the output end of the pressure-reducing vacuum dewatering mechanism 24 is communicated with the input end of the filtering mechanism 26 through a pipeline, the six-solenoid valve 25 is arranged on the connecting pipeline, and the output end of the filtering mechanism 26 is communicated with the next working procedure.
A liquid level probe 27 is arranged at the upper part of a water distribution tank 13 in the device, a liquid level meter 15 is arranged at one side of the water distribution tank 13, and the liquid level meter 15 is communicated with the inner space of the water distribution tank 13.
A first metering pump 3, a second metering pump 7, a first centrifugal pump 20, a second centrifugal pump 23, a stirring motor 10, a first flow meter 4, a second flow meter 8, a liquid level probe 27, a first electromagnetic valve 2, a second electromagnetic valve 6, a third electromagnetic valve 18, a fourth electromagnetic valve 19, a fifth electromagnetic valve 22 and a sixth electromagnetic valve 25 in the device are respectively connected with a control console 28 through data lines.
Examples
1. Inputting process parameters: before use, technological parameters of a first metering pump 3, a second metering pump 7, a stirring motor 10, a first flowmeter 4, a second flowmeter 8, a first centrifugal pump 20, a second centrifugal pump 23, a first electromagnetic valve 2, a second electromagnetic valve 6, a third electromagnetic valve 18, a fourth electromagnetic valve 19, a fifth electromagnetic valve 22, a sixth electromagnetic valve 25 and a liquid level probe 27 are input into a control console 28.
2. Conveying mixed oil water: the control console 28 sends an instruction to open the first electromagnetic valve 2 and the first metering pump 3, mixed oil water in the mixed oil water tank 1 is pumped into the water distribution tank 13 through a pipeline, the first flowmeter 4 arranged on the pipeline is used for controlling and monitoring the adding amount of the mixed oil water, the liquid level meter 15 is used for observing the liquid level condition in the water distribution tank 13, when the liquid level probe 27 detects that the mixed oil water in the water distribution tank 13 reaches the process requirement, the liquid level probe 27 sends a signal to the control console 28, the control console 28 sends an instruction to close the first electromagnetic valve 2 and the first metering pump 3, the mixed oil water injection into the water distribution tank 13 is stopped, the mixed oil water in the water distribution tank 13 is heated, and the heating temperature is controlled to be 40-80 ℃.
3. Conveying of liquid medicine: when the heating in the water diversion tank 13 meets the process requirements, the console 28 sends an instruction, the second electromagnetic valve 6 and the second metering pump 7 are opened, Polyacrylamide (PAM) aqueous solution with the mass percentage concentration of 1% in the flocculant storage tank 5 is pumped into the water diversion tank 13 through the second metering pump 7 through a pipeline according to the amount of 1/10 added of mixed oil water, namely the weight ratio of the liquid medicine to the mixed oil water is 1:10, and the second flowmeter 8 arranged on the connecting pipeline is used for controlling and monitoring the added amount of the liquid medicine.
4. Stirring the mixed solution: after the liquid medicine is added, the console 28 sends an instruction to close the second electromagnetic valve 6 and the second metering pump 7, the liquid medicine injection into the water distribution tank 13 is stopped, the stirring motor 10 mounted on the mounting frame 9 is driven to work, the stirring motor 10 drives the speed reducer 11 to rotate, the speed reducer 11 drives the stirring shaft 12 and the blades 14 connected with the speed reducer 11 to stir and separate the mixed liquid in the water distribution tank 13, the stirring time is 3-10 minutes, and the mixed liquid is kept stand for 30-120 minutes after the stirring is completed, so that the water, the slag and the grease clarifying liquid at the lower layer of the water distribution tank 13 are separated.
5. Discharge of sewage and residue: after the separation is completed, the console 28 sends an instruction to open the third electromagnetic valve 18 arranged on a pipeline connected with the sewage treatment station 17 at the bottom of the water distribution tank 13, water and residues generated in the lower layer of the water distribution tank 13 are discharged into the sewage treatment station 17 through the pipeline for treatment, the discharge condition of the water and the residues is monitored through the observation window 16, when the water and the residues are observed to be discharged, the console 28 sends an instruction to close the third electromagnetic valve 18, simultaneously open the fourth electromagnetic valve 19 and the first centrifugal pump 20, and pump grease clarifying solution into the collection tank 21 for later use.
6. Treating the grease clarified liquid: the console 28 sends an instruction to open a fifth electromagnetic valve 22 and a second centrifugal pump 23 which are arranged on the connecting pipeline, the grease clarified liquid is input into the decompression vacuum dehydration mechanism 24 for further dehydration treatment, then the console 28 sends an instruction to open a sixth electromagnetic valve 25, the grease clarified liquid treated by the decompression vacuum dehydration mechanism 24 is conveyed into the filtering mechanism 26 for filtering treatment, the trace residue contained in the grease clarified liquid is filtered, and the qualified finished grease without residue and water is obtained after the filtering treatment.
The above description is only a non-limiting embodiment of the present invention, and many embodiments can be derived, and it will be apparent to those skilled in the art that many modifications and improvements can be made without departing from the inventive concept and without making creative efforts, and these embodiments are all within the protection scope of the present invention.
Claims (3)
1. A contain quick oil-water separator of miscellaneous soap-containing emulsified oil, includes: mix profit storage tank (1), solenoid valve (2), a measuring pump (3), a flowmeter (4), flocculating agent storage tank (5), No. two solenoid valves (6), No. two measuring pumps (7), No. two flowmeter (8), agitator motor (10), speed reducer (11), (mixing) shaft (12), divide water jar (13), blade (14), level gauge (15), observation window (16), No. three solenoid valves (18), No. four solenoid valves (19), a centrifugal pump (20), collection tank (21), No. five solenoid valves (22), No. two centrifugal pump (23), decompression vacuum dehydration mechanism (24), No. six solenoid valves (25), filtering mechanism (26), liquid level probe (27) and control cabinet (28), its characterized in that: a mixed oil-water storage tank (1) in the device is communicated with the input end of a first metering pump (3) through a pipeline, a first electromagnetic valve (2) is arranged on a connecting pipeline, the output end of the first metering pump (3) is communicated with a water distribution tank (13) through a pipeline, a first flowmeter (4) is arranged on the connecting pipeline, a flocculating agent storage tank (5) is communicated with the input end of a second metering pump (7) through a pipeline, a second electromagnetic valve (6) is arranged on the connecting pipeline, the output end of the second metering pump (7) is communicated with the water distribution tank (13) through a pipeline, a stirring motor (10) is arranged on an installation frame (9) at the top of the water distribution tank (13), a speed reducer (11) is arranged on an output shaft of the stirring motor (10), an output shaft of the speed reducer (11) is connected with a stirring shaft (12) provided with blades (14, the pipeline is communicated with a sewage treatment station (17), a third electromagnetic valve (18) is arranged on the connecting pipeline, the connecting pipeline is communicated with the input end of a first centrifugal pump (20) through a three-way pipe, a fourth electromagnetic valve (19) is arranged on the connecting pipeline, the output end of the first centrifugal pump (20) is communicated with a collecting tank (21) through a pipeline, the lower part of the collecting tank (21) is communicated with the input end of a second centrifugal pump (23) through a pipeline, a fifth electromagnetic valve (22) is arranged on the connecting pipeline, the output end of the second centrifugal pump (23) is communicated with the input end of a pressure reduction vacuum dehydration mechanism (24) through a pipeline, the output end of the pressure reduction vacuum dehydration mechanism (24) is communicated with the input end of a filtering mechanism (26) through a pipeline, a sixth electromagnetic valve (25) is arranged on the connecting pipeline, and the output end of.
2. The device for rapidly separating oil and water from the miscellaneous emulsified oil containing soap according to claim 1, wherein: a liquid level probe (27) is arranged at the upper part of a water distribution tank (13) in the device, a liquid level meter (15) is arranged at one side of the water distribution tank (13), and the liquid level meter (15) is communicated with the inner space of the water distribution tank (13).
3. The device for rapidly separating oil and water from the miscellaneous emulsified oil containing soap according to claim 1, wherein: a first metering pump (3), a second metering pump (7), a first centrifugal pump (20), a second centrifugal pump (23), a stirring motor (10), a first flow meter (4), a second flow meter (8), a liquid level probe (27), a first electromagnetic valve (2), a second electromagnetic valve (6), a third electromagnetic valve (18), a fourth electromagnetic valve (19), a fifth electromagnetic valve (22) and a sixth electromagnetic valve (25) in the device are respectively connected with a control console (28) through data lines.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN110228871A (en) * | 2019-07-15 | 2019-09-13 | 新锦龙生物基材料（湖北）有限公司 | A kind of method and device of the quick water-oil separating containing miscellaneous oil emulsion containing soap |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN110228871A (en) * | 2019-07-15 | 2019-09-13 | 新锦龙生物基材料（湖北）有限公司 | A kind of method and device of the quick water-oil separating containing miscellaneous oil emulsion containing soap |
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