Turbine oil demulsification degree detection device

By designing a turbine oil deemulsion detection device and using the measurement module to monitor the emulsion status in the constant temperature device, the problem of insufficient detection accuracy in the prior art is solved, and rapid and accurate deemulsion detection is achieved, and the quality and production efficiency of oil products are improved.

CN223006023UActive Publication Date: 2025-06-20中电华创(苏州)电力技术研究有限公司 +1
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Patent Information

Application Number
CN202421113898.9
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-05-21
Publication Date
2025-06-20
Estimated Expiration
2034-05-21

AI Technical Summary

Technical Problem

In the prior art, there is a problem of insufficient accuracy in the detection method for the degree of emulsification of turbine oil, resulting in inaccurate results.

Method used

A turbine oil deemulsification detection device is designed, including a main control module, a reaction module, a constant temperature device and a measurement module. The measurement module monitors the emulsion status in the constant temperature device and records the test signal time feedback from the measurement module to quickly obtain the degree of emulsification.

Benefits of technology

It realizes rapid and accurate detection of the deemulsification degree of turbine oil, and improves the guarantee of oil quality and production efficiency.

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Abstract

The utility model provides a turbine oil demulsification degree detection device. The turbine oil demulsification degree detection device comprises a main control module, a reaction module, a constant temperature device and a measurement module, the main control module is electrically connected with the constant temperature device and the measuring module, and the main control module is used for driving the measuring module and the constant temperature device to operate and recording the time of a test signal sent by the measuring module; the reaction module is used for preparing emulsion; the constant temperature device is used for providing a constant temperature environment for the reaction module, and the measurement module is arranged in the constant temperature device so as to monitor the oil-water separation condition of the emulsion in the constant temperature device and feed back the test signal to the main control module. According to the utility model, the state of the emulsion in the constant temperature device is monitored under the action of the measuring module, and after the measuring module feeds back a test signal, an operator can record the feedback time of the monitoring signal according to the main control device so as to quickly obtain the demulsification degree of the corresponding turbine oil.
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Description

Technical Field

[0001] The utility model belongs to the technical field of demulsification degree detection, and particularly relates to a device for detecting the demulsification degree of turbine oil. Background Art

[0002] The demulsification degree refers to the time for water-oil separation measured under specified experimental conditions when an emulsion is formed by mixing oil and water, which is one of the main indicators for measuring the water-oil separation performance of oil products. During the operation of a turbine, if the water content in its lubricating oil system exceeds the standard, emulsification will occur under the action of surfactants and agitation, thus destroying the oil film on the metal surface. In addition, it is also prone to cause corrosion of metal components, accelerate the aging of oil products, and generate oil sludge. As an important indicator of turbine oil, the rapid and accurate detection of the demulsification degree is of great significance for ensuring the quality of oil products and improving production efficiency. At present, the detection of the demulsification degree of turbine oil is usually carried out by manual sampling, and the time is recorded after visually judging the water-oil separation. This measurement method has certain limitations and the results are not accurate. Content of the Utility Model

[0003] In order to solve the problem that the existing method for detecting the demulsification degree of turbine oil in the background art has certain inaccuracies, the utility model proposes the following technical solutions:

[0004] A device for detecting the demulsification degree of turbine oil includes: a main control module, a reaction module, a constant temperature device, and a measurement module; the main control module is electrically connected to the constant temperature device and the measurement module respectively. The main control module is used to drive the measurement module and the constant temperature device to operate, and record the time of the test signal sent by the measurement module; the reaction module is used to prepare an emulsion; the constant temperature device is used to provide a constant temperature environment for the reaction module, and the measurement module is arranged in the constant temperature device to monitor the water-oil separation situation of the emulsion in the constant temperature device and feedback the test signal to the main control module.

[0005] Among them, the reaction module includes: a first solution storage bottle, a second solution storage bottle, a third solution storage bottle, a liquid transfer pump, and a reactor; one end of the liquid transfer pump is respectively connected to the first solution storage bottle, the second solution storage bottle, and the third solution storage bottle through electromagnetic valves, and the other end of the liquid transfer pump is connected to the reactor through a pipeline; the reactor is placed in the constant temperature device, and the height of the reactor is greater than the liquid level height of the solution in the constant temperature device.

[0006] Further, the constant temperature device includes: a water bath, a heater, and a temperature sensor; an aqueous solution and the reactor are carried in the water bath, the measurement module is fixedly provided on the outer peripheral surface of the water bath, the heater is provided on the outer bottom surface of the water bath, and the temperature sensor is provided on the inner side wall of the water bath; the heater and the temperature sensor are both connected to the main control module to stabilize the solution temperature in the water bath.

[0007] Further, the measurement module includes: a monochromatic light generator, a laser generator, a refractometer, and a photometer; the monochromatic light generator and the laser generator are respectively fixedly provided on the inner peripheral wall of the water bath; the refractometer is used to receive the emission signal of the laser generator and feedback a refractive index signal to the main control module; the photometer is used to receive the monochromatic light generator and feedback an absorbance signal to the main control module.

[0008] Further, the connection line between the emission point of the monochromatic light generator and the photometer is perpendicular to and intersects the central axis of the reactor.

[0009] Further, the connection line between the emission point of the monochromatic light generator and the photometer is located below the liquid level at the water-oil separation junction in the reactor, and the connection line between the emission point of the laser generator and the refractometer intersects the connection line between the emission point of the monochromatic light generator and the photometer.

[0010] Further, a cleaning module is further included; the cleaning module includes: a waste liquid storage tank and an ultrasonic generator; the waste liquid storage tank is provided outside the water bath, and the waste liquid storage tank is connected to the reactor through a drain pump; the ultrasonic generator is provided on the outer bottom surface of the water bath, and the ultrasonic generator is electrically connected to the main control module to perform ultrasonic cleaning on the reactor.

[0011] Beneficial effects: The present utility model monitors the state of the emulsion in the constant temperature device through the action of the measurement module. After the measurement module feeds back the test signal, the operator can quickly obtain the demulsification degree of the corresponding emulsion according to the feedback time of the monitoring signal recorded by the main control device. Description of the Drawings

[0012] Figure 1 It is a framework diagram of a turbine oil demulsification degree detection device according to an embodiment of the present utility model. Detailed Embodiments

[0013] In order to make the objectives, technical solutions, and advantages of the present application clearer, the present utility model will be further described in detail below with reference to the drawings. It should be understood that the specific embodiments described herein are only used to explain the present utility model and are not used to limit the present utility model.

[0014] It should be understood that the orientation or positional relationship indicated by terms such as "center", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", etc. is based on the orientation or positional relationship shown in the drawings. It is only for the convenience of describing this patent and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation. Therefore, it should not be construed as a limitation to this patent.

[0015] Figure 1 It is a framework diagram of a turbine oil demulsification degree detection device according to an embodiment of the present invention.

[0016] Refer to Figure 1 , according to the embodiment of the present invention Figure 1 A turbine oil demulsification degree detection device according to an embodiment of the present invention includes: a main control module 1, a reaction module 2, a constant temperature device 3, and a measurement module 4. The main control module 1 is electrically connected to the constant temperature device 3 and the measurement module 4 respectively. The main control module 1 is used to drive the measurement module 4 and the constant temperature device 3 to operate, and record the time when the measurement module 4 sends a test signal. The reaction module 2 is used to prepare an emulsion. The constant temperature device 3 is used to provide a constant temperature environment for the reaction module 2. The measurement module 4 is arranged in the constant temperature device 3 to monitor the state of the emulsion in the constant temperature device 3 and feedback a test signal to the main control module 1.

[0017] Specifically, the reaction module 2 includes: a first solution storage bottle 21, a second solution storage bottle 22, a third solution storage bottle 23, a pipette pump 24, and a reactor 25. Among them, one end of the pipette pump 24 is respectively connected to the first solution storage bottle 22, the second solution storage bottle 23, and the third solution storage bottle 24 through a solenoid valve 26, and the other end of the pipette pump 24 is connected to the reactor 27. The reactor 27 is arranged in the constant temperature device 3, and the height of the reactor is greater than the liquid level height of the solution in the constant temperature device.

[0018] Under the quantitative control of the solenoid valve, the pipette pump 24 can extract a quantitative solution from the first solution storage bottle 21 and the second solution storage bottle 22 respectively, so as to form an emulsion in the reactor 27. Among them, the first solution storage bottle 21, the second solution storage bottle 22, and the third solution storage bottle 23 store oil samples, water, and cleaning agents respectively. Preferably, in other embodiments, corresponding telescopic rods and stirrers 6 and other devices can also be arranged in the reactor 25 to accelerate the formation speed of the emulsion in the reactor.

[0019] Specifically, the measurement module 4 includes: a monochromatic light generator 41, a laser generator 42, a refractometer 43, and a photometer 44. The monochromatic light generator 41 and the laser generator 42 are respectively fixed on the inner peripheral wall of the water bath 31, and the refractometer and the photometer are respectively fixed on the outer peripheral wall of the water bath 31. Among them, the monochromatic light generator 41 is located below the laser generator 42. The emission signal of the monochromatic light generator 41 is received by the photometer 43, and the emission signal of the laser generator 42 is received by the refractometer 44. The connection line between the emission point of the monochromatic light generator 41 and the photometer 44 is perpendicular to the central axis of the reactor 25. The connection line between the emission point of the monochromatic light generator 41 and the photometer 44 is located below the liquid level in the reactor 25, and the connection line between the emission point of the laser generator 42 and the emission point of the refractometer 43 intersects with the connection line between the emission point of the monochromatic light generator 41 and the photometer 44. Preferably, in order to further accelerate the detection speed, the volume of the part of the solution level in the reactor 25 that is higher than the connection line between the emission point of the monochromatic light generator 41 and the photometer 44 is greater than 3 cubic centimeters.

[0020] Specifically, the photometer 44 is used to receive the emission signal of the monochromatic light generator 41 and obtain the absorbance of the corresponding solution, so as to feedback the absorbance signal to the main control module 1. The refractometer 45 is used to receive the emission signal of the laser generator 42 and obtain the refractive index of the corresponding solution, so as to feedback the refractive index signal to the main control module 1. Preferably, in other embodiments, in order to further improve the signal propagation effect, the measurement module 4 further includes a signal amplifier. The detection ends of the signal amplifier are respectively connected to the output of the monochromatic light generator 41 and the output end of the laser generator 42, so as to jointly form a test signal with the absorbance signal and the refractive index signal.

[0021] Among them, before preparing the emulsion in the reactor 25, the measurement module 4 first obtains the absorbance signal and the refractive index signal of the solution in the reactor 25 and feeds them back to the main control module 1. The main control module 1 records the absorbance and refractive index at this time as the stable state values. When performing the demulsification degree test, the operator determines the demulsification degree of the corresponding turbine oil by finding the time when the absorbance and refractive index of the emulsion in the test signal obtained by the main control module first return to the stable state values.

[0022] Specifically, the constant temperature device 3 includes: a water bath 31, a heater 32, and a temperature sensor 33. The heater 32, the temperature sensor 33, and the ultrasonic generator 34 are electrically connected to the main control module 1. Under the command of the main control device 1, the heater 32 is powered on to generate heat, so as to heat the aqueous solution in the water bath 31. The temperature sensor 33 controls the magnitude and stop of the heating according to the set temperature value, so as to provide a constant temperature environment for the emulsion in the reactor 27 in the water bath 31.

[0023] To quickly conduct multiple demulsification detection experiments on different turbine oils, a turbine oil demulsification detection device of the present application further includes: a cleaning module 5. Among them, the cleaning module 5 includes: a waste liquid storage tank 51 and an ultrasonic generator 52. The waste liquid storage tank 51 is arranged outside the water bath 31, and the waste liquid storage tank 51 is connected to the reactor 25 through a drain pump 53. The ultrasonic generator 52 is fixedly arranged on the outer bottom surface of the water bath 31, and the ultrasonic generator 52 is controlled by the main control module 1. After the demulsification test is completed, the main control module 1 starts the ultrasonic generator 52 to perform ultrasonic cleaning on the inside of the reactor 25. After the cleaning is completed, the main control module 1 controls the drain pump 53 to extract the solution in the reactor and discharge it into the waste liquid storage tank 51, thereby achieving the purpose of sustainable multiple tests.

[0024] In summary, the present utility model monitors the state of the emulsion in the constant temperature device through the action of the measurement module. After the measurement module feeds back the test signal, the operator can quickly obtain the demulsification degree of the corresponding emulsion according to the feedback time of the monitoring signal recorded by the main control device.

[0025] The specific embodiments of the utility model have been described above. Other embodiments are within the scope of the appended claims.

[0026] The terms "exemplary", "example", etc. used throughout this specification mean "serving as an example, instance, or illustration", and do not mean "preferred" or "having an advantage" over other embodiments. For the purpose of providing an understanding of the described technology, the detailed description includes specific details. However, these technologies can be implemented without these specific details. In some instances, well-known structures and devices are shown in block diagram form to avoid obscuring the concepts of the described embodiments.

[0027] The above has described in detail the optional implementation manners of the embodiments of the present utility model in conjunction with the drawings. However, the embodiments of the present utility model are not limited to the specific details in the above implementation manners. Within the technical concept scope of the embodiments of the present utility model, various simple modifications can be made to the technical solutions of the embodiments of the present utility model, and these simple modifications all belong to the protection scope of the embodiments of the present utility model.

[0028] The above description of the content of this specification is provided to enable any ordinary person skilled in the art to implement or use the content of this specification. For those of ordinary skill in the art, various modifications to the content of this specification are obvious, and the general principles defined herein can also be applied to other variations without departing from the protection scope of the content of this specification. Therefore, the content of this specification is not limited to the examples and designs described herein, but is consistent with the broadest scope that conforms to the principles and novel features disclosed herein.

Claims

1. A turbine oil demulsification detection device, characterized in that: include: A main control module (1), a reaction module (2), a constant temperature device (3) and a measuring module (4); the main control module (1) is electrically connected to the constant temperature device (3) and the measuring module (4) respectively, the main control module (1) is used to drive the measuring module (4) and the constant temperature device (3) to operate, and to record the time of the test signal sent by the measuring module (4); the reaction module (2) is used to prepare an emulsion; the constant temperature device (3) is used to provide a constant temperature environment for the reaction module (2), and the measuring module (4) is arranged in the constant temperature device (3) to monitor the oil-water separation of the emulsion in the constant temperature device (3) and to feed back the test signal to the main control module (1).

2. A turbine oil demulsification degree detection device according to claim 1, characterized in that: The reaction module (2) comprises: a first solution storage bottle (21), a second solution storage bottle (22), a third solution storage bottle (23), a liquid transfer pump (24), and a reactor (25); one end of the liquid transfer pump (24) is connected to the first solution storage bottle (21), the second solution storage bottle (22), and the third solution storage bottle (23) respectively through an electromagnetic valve (26), and the other end of the liquid transfer pump (24) is connected to the reactor (25) through a pipeline; the reactor (25) is placed in the constant temperature device (3), and the height of the reactor (25) is greater than the liquid level of the solution in the constant temperature device (3).

3. A turbine oil demulsification degree detection device according to claim 2, characterized in that: The constant temperature device (3) comprises: a water bath (31), a heater (32) and a temperature sensor (33); the water bath (31) carries an aqueous solution and the reactor (25); the measuring module (4) is fixedly provided on the outer peripheral surface of the water bath (31); the heater (32) is provided on the outer bottom surface of the water bath (31); and the temperature sensor (33) is provided on the inner side wall of the water bath (31); the heater (32) and the temperature sensor (33) are both connected to the main control module (1) to stabilize the temperature of the solution in the water bath (31).

4. A turbine oil demulsification degree detection device according to claim 3, characterized in that: The measuring module (4) comprises: a monochromatic light generator (41), a laser generator (42), a photometer (43), and a refractometer (44); the monochromatic light generator (41) and the laser generator (42) are respectively fixed on the inner wall of the water bath (31); the refractometer (44) is used to receive the emission signal of the laser generator (42) and to feed back the refractive index signal to the main control module (1); the photometer (43) is used to receive the monochromatic light generator (41) and to feed back the absorbance signal to the main control module (1).

5. A turbine oil demulsification degree detection device according to claim 4, characterized in that: The line connecting the emission point of the monochromatic light generator (41) and the photometer (43) intersects perpendicularly with the central axis of the reactor (25).

6. A turbine oil demulsification degree detection device according to claim 5, characterized in that: The line connecting the emission point of the monochromatic light generator (41) and the photometer (43) is located below the liquid surface at the water-oil separation interface in the reactor (25), and the line connecting the emission point of the laser generator (42) and the refractometer (44) intersects with the line connecting the emission point of the monochromatic light generator (41) and the photometer (43).

7. A turbine oil demulsification degree detection device according to claim 5, characterized in that: The invention also comprises a cleaning module (5); the cleaning module (5) comprises: a waste liquid storage tank (51) and an ultrasonic generator (52); the waste liquid storage tank (51) is arranged outside the water bath (31), and the waste liquid storage tank (51) is connected to the reactor (25) via a liquid discharge pump; the ultrasonic generator (52) is arranged on the outer bottom surface of the water bath (31), and the ultrasonic generator (52) is electrically connected to the main control module (1) so as to perform ultrasonic cleaning on the reactor (25).

Citation Information

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