CN211291499U - Real-time online detection system for multi-component volume ratio in fluid output process - Google Patents
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Abstract
The utility model discloses a belong to the technical field of fluid multicomponent volume ratio detection, specifically be a real-time on-line measuring system of multicomponent volume ratio of fluid output process, including positive displacement flow sensor, programmable logic controller PLC and storage module, positive displacement flow sensor's output passes through the data line and is connected with programmable logic controller PLC's input, programmable logic controller PLC passes through the data line and storage module electric connection; the storage module comprises six common storage units, the six common storage units are respectively SUA1, SUA2, SDA, SUB1, SUB2 and SDB, zero points of sampling sections at each time are signals acquired at the previous moment and are subjected to program operation, so that the real-time flow and flow speed at the current moment can be obtained, a large amount of storage space is also avoided to be occupied, in addition, the sampling time interval is also reasonably set, and the sampling time interval is as short as possible; the accuracy of detection is improved.
Description
Technical Field
The utility model relates to a fluid multicomponent volume ratio detects technical field, specifically is a real-time on-line measuring system of multicomponent volume ratio of fluid output process.
Background
The multi-component fluid mixing ratio output is more and more applied to various industries, and the key control indexes of the multi-component fluid mixing quality are as follows: the proportioning (100: XX) is commonly used by weight ratio and volume ratio. Wherein the weight ratio can be obtained by weighing, whereas the volume ratio, especially when the viscosity of the fluid is high, can only be obtained by detection by the device and the corresponding sensor.
The current volume ratio detection method is: the flow rate of each fluid is detected by a sensor (such as a volume flow sensor) and a Programmable Logic Controller (PLC), and then the volume proportion of the fluid proportion is calculated, but the difficulty is the acquisition of real-time volume proportion, and the key point is the detection of the real-time flow rate of each fluid participating in proportion mixing.
The current widely used fluid flow detection instruments or systems operate in the following modes: the sensor sends out an analog signal (pulse), the detection system reads the pulse at certain time intervals, and then the flow rate is calculated according to the specific equivalent of each pulse. However, the characteristics of the fluid itself, the precision of the components such as the pump and the valve, etc., often cause the fluid to flow dynamically and fluctuate, which is a great challenge for the currently adopted volume ratio detection system, the current detection system cannot timely and accurately reflect the real-time flow rate and the change of the flow rate, and although the current technology can calculate the real-time flow rate data by adopting the encrypted acquisition times, the real-time validity and the accuracy of the value cannot be guaranteed because the zero point of the measurement cannot be changed in real time. If real-time flow is not available, the exact real-time volume fraction is naturally not available, so we have developed this technique for this situation.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a real-time on-line measuring system of multicomponent volume ratio of fluid output process to the zero point of the measurement of proposing in solving above-mentioned background art can't change in real time, therefore real-time validity, the accuracy of numerical value still can't guarantee, and real-time flow can't obtain, can't obtain the problem of accurate real-time volume ratio naturally.
In order to achieve the above object, the utility model provides a following technical scheme: a real-time online detection system for multi-component volume ratio in a fluid output process comprises a volume flow sensor, a Programmable Logic Controller (PLC) and a storage module, wherein the output end of the volume flow sensor is connected with the input end of the PLC through a data line, and the PLC is electrically connected with the storage module through the data line;
the storage module comprises six common storage units, wherein the six common storage units are SUA1, SUA2, SDA, SUB1, SUB2 and SDB.
Preferably, the programmable logic controller PLC is connected with at least two volume type flow sensors.
Preferably, the real-time online detection system for the multi-component volume ratio of the fluid output process further comprises a display, and the display is connected with the Programmable Logic Controller (PLC) through a data line.
Compared with the prior art, the beneficial effects of the utility model are that:
1) the zero point of each sampling section is the signal acquired at the previous moment and program operation is carried out, so that the real-time flow and flow speed at the current moment can be obtained, a large amount of storage space is also avoided, in addition, the sampling time interval is reasonably set, and the sampling time interval is as short as possible;
2) the accuracy of detection is improved.
Drawings
FIG. 1 is a logic block diagram of the system of the present invention;
fig. 2 is a system logic block diagram of the storage module of the present invention;
fig. 3 is a result diagram of the recorded data of the present invention.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
In the description of the present invention, it is to be understood that the terms "upper", "lower", "front", "rear", "left", "right", "top", "bottom", "inner", "outer", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplicity of description, and do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore, should not be construed as limiting the present invention.
Example (b):
referring to fig. 1-3, the present invention provides a technical solution: a real-time online detection system for multi-component volume ratio in a fluid output process comprises a volume flow sensor, a Programmable Logic Controller (PLC) and a storage module, wherein the output end of the volume flow sensor is connected with the input end of the PLC through a data line, and the PLC is electrically connected with the storage module through the data line;
the Programmable Logic Controller (PLC) is connected with at least two volume type flow sensors, the volume type flow sensors are arranged on a conveying pipeline of target fluid, and the Programmable Logic Controller (PLC) also comprises a display, and the display is connected with the Programmable Logic Controller (PLC) through a data line;
the storage module comprises six common storage units, wherein the six common storage units are respectively SUA1, SUA2, SDA, SUB1, SUB2 and SDB;
the key of the real-time online detection system of the multi-component volume ratio in the fluid output process is the detection of the flow rate of each fluid participating in the matching and mixing. The method of manual weighing measurement is not considered because it cannot be performed on-line, and therefore only a programmable detection system is used.
The automatic detection technology is characterized in that a volume type flow sensor is adopted, corresponding pulse signals are generated and sent out corresponding to a certain volume, an acquisition system is responsible for acquiring the pulse signals and counting, then the system calculates according to a certain rule to obtain flow based on sampling time, A, B groups of fluids are supposed to participate in proportioning and mixing in the process of target fluid, and KA and KB are K coefficients of the flow sensors of the A loop and the B loop respectively, and the specific conditions are as follows:
a (0) is zero sensor data of the component A fluid, then the sampling is carried out under the control of the system to obtain A (1), A (2), A (3), A (4) and the like, and then the flow rate at the corresponding moment is obtained through corresponding calculation: QA (1) ═ a (1) -a (0)) × KA, Q (2) ═ a (2) -a (0)) × KA, Q (3) ═ a (3) -a (0)) × KA, Q (4) ═ a (4) -a (0)) × KA, and the like;
b (0) is zero sensor data of the component B fluid, B (1), B (2), B (3), B (4) and the like, and then the flow rate at the corresponding moment is obtained through corresponding calculation: QB (1) ═ B (1) -B (0)) × KB, QB (2) ═ B (2) -B (0)) × KB, QB (3) ═ B (3) -B (0)) × KB, QB (4) ═ B (4) -B (0)) × KB, and the like;
then calculating RB (n) ═ QB (n) × 100/QA (n), and obtaining A, B with the mixture ratio of 100: RB (n);
it can be seen here that the flow rate detection of the A, B fluid is very important, and directly affects the calculation result of the mixture ratio, so the detection of the online volume ratio is firstly to ensure the detection accuracy and acquisition of the real-time flow rate.
However, the current flow measurement metering method is suitable for a constant flow rate, and a large deviation occurs for a dynamic fluid, which is described as follows:
at constant flow rate:
according to the current flow rate detection method, taking the fluid a as an example, n sampling segments share the zero point a (0) of the first sampling segment, after n +1 sampling segments, the system and the program update the zero point to a (n), and then obtain the flow rates Q (n +1) ═ a (n +1) -a (n) KA, Q (n +2) ═ a (n +2) -a (n) KA, Q (n +3) ═ a (n) KA, … … according to the same method, and the zero points of the subsequent sampling segments are all a (n) KA.
Assuming that the time interval T of each sampling is constant, if the flow rate f (n) of the fluid is also constant, the calculated flow rate is:
f (n) ═ Q (n +1)/1 × T, F (n +1) ═ Q (n +2)/2 × T, … …; the flow rates obtained at the various times are the same and the existing methods are acceptable for constant flow rates.
However, in reality, the flow rate of the fluid is dynamically changed in real time, and the constant flow rate of the fluid is difficult to occur in practical applications in consideration of the manufacturing of the components, the control accuracy, and the influence of various factors. Therefore, the accurate and timely metering of the flowing process of the dynamic fluid is very important for ensuring the proportioning quality of the multi-component fluid. Moreover, the real-life fluctuation is also caused by abnormity, defects and abrasion, and serious accidents and faults of equipment or systems are caused after long-term accumulation.
In case of dynamic flow rate:
for the detected fluid process is dynamic, the online detection of the fluid flow usually requires a program to set a plurality of sampling segments, and our detection method is based on a plurality of sampling segments, and the zero point of each sampling segment is refreshed in each sampling segment, so as to obtain the real-time flow rate FRA (), FRB () and flow QRA (), QRB () as follows:
QRA (n +1) ═ a (n +1) -a (n)) × KA, QRA (n +2) ═ a (n +2) -a (n +1)) × KA, QRA (n +3) ═ a (n +3) -a (n +2)) × KA, … …; and the flow rate: FRA (n +1) ═ QR (n +1)/T (n +1), FRA (n +2) ═ QR (n +2)/T (n +2), FRA (n +3) ═ QR (n +2)/T (n +3), … …;
if the dynamic fluid process is sampled in sections, the following results are obtained:
a (0) × KA ═ 0, a (1) × KA ═ 0.5, a (2) × KA ═ 0.5, a (3) × KA ═ 3.0, a (4) × KA ═ 6.0, the time intervals T are all 1 second, and the equivalent of the sensor is also set to 1 for the sake of simplicity, note that the same values are found in sections a (1) and a (2), which means that the section a (2) has virtually no flow output; and (3) corresponding to the component B: b (0) × KB ═ 0, B (1) × KB ═ 0.3, B (2) × KB ═ 0.35, B (3) × KB ═ 2.0, B (4) × KB ═ 3.5;
the real-time flow and flow rate values obtained by zero-point segment-by-segment real-time refreshing are respectively as follows:
the same number of acquisitions { interval 1 second }: a (0) × KA ═ 0, a (1) × KA ═ 0.5, a (2) × KA ═ 0.5, a (3) × KA ═ 3.0, a (4) × KA ═ 6.0;
QRA(1)＝A(1)-A(0)，QRA(2)＝A(2)-A(1)，QRA(3)＝A(3)-A(2)，
QRA(4)＝A(4)-A(3)；
QRA(1)＝0.5QRA(2)＝0.1QRA(3)＝2.4QRA(4)＝3.0；
FRA(1)＝0.5FRA(2)＝0.1FRA(3)＝2.4FRA(4)＝3.0；
the real-time flow and the real-time flow rate of the component B can be obtained by the same method:
b (0) × KB ═ 0, B (1) × KB ═ 0.3, B (2) × KB ═ 0.35, B (3) × KB ═ 2.0, B (4) × KB ═ 3.5, and the sampling interval is 1;
QRB(1)＝0.3QRB(2)＝0.05QRB(3)＝1.65QRB(4)＝1.5；
FRB(1)＝0.3FRB(2)＝0.05FRB(3)＝1.65FRB(4)＝1.5；
however, when using the current method (i.e., the zero points of the n sampling segments sharing the first sampling segment are both a (0) and B (0)) to obtain flow and velocity values:
A(0)*KA＝0,A(1)*KA＝0.5,A(2)*KA＝0.5,A(3)*KA＝3.0,A(4)*KA＝6.0；
B(0)*KB＝0,B(1)*KB＝0.3,B(2)*KB＝0.35,B(3)*KB＝2.0,B(4)*KB＝3.5；
QA(1)＝0.5QA(2)＝0.6QA(3)＝3.0QA(4)＝6.0；
QB(1)＝0.3QB(2)＝0.35QB(3)＝2.0QB(4)＝3.5；
if the control index is 58 + -2, then:
by the current metering method, whether the fluid is collected for multiple times or collected for a single time, most of the target fluid process is qualified, and although the multi-section detection only finds that one section of control index is unqualified, the whole 2-component fluid output process can be judged to meet the requirement of the control index according to the current detection result;
however, with our zero real-time refresh and multi-stage detection method, the remaining working stages are not qualified except for the initial stage, so that the entire fluid output is not qualified in practice and the fluid process needs to be adjusted or overhauled. If the device is left, the device can cause hidden dangers and even serious accidents or faults.
Therefore, the current metering and detecting method cannot truly and accurately reflect the real flow and the rotating speed of the actual fluid process, so that the real indexes of the proportioning of the multi-component fluid process cannot be truly reflected, even covering and compromising serious deviation can cause uncontrollable quality and accidents.
In addition, automatic control and even closed-loop control are widely applied in practice, the control mechanisms can automatically make up for the fluctuation in a reverse direction, the system operation is very stable by adopting the current metering and detecting method (the zero point is uniform and unchanged), the fluctuation exists all the time and is alternatively made up, some fluctuation is in a required range, but the fluctuation always exceeds the required range along with factors such as the abrasion of parts and the like, so that hidden danger in operation is caused, and the mixing ratio of the multi-component fluid is a key control index, so that the mixing volume ratio of the fluid can be accurately detected in real time on line, and is very necessary.
The liquid dynamic flow detection system with zero point refreshing is composed of a positive displacement sensor and a Programmable Logic Controller (PLC).
By means of a Programmable Logic Controller (PLC) and corresponding programming, zero point refreshing at each sampling moment is realized by program setting, which specifically comprises the following steps:
1. the program sets up and defines 6 common storage units as SUA1 and SUA2, SDA, SUB1 and SUB2, SDB, respectively;
2. the program defines a loop execution module comprising the operations of:
acquisition of the specific sensor signals (number of pulses) A (n)
-storing the values a (n) collected in SUA2 and calculating SUA2-SUA 1-SDA
-storing the value b (n) collected in SUB2 and calculating SUB2-SUB1 ═ SDB
-calculating the real-time ratio: ra (n) ═ (SDB KB 100)/(SDA KA)
-performing real-time flow and velocity calculations
Assigning a value of SUA2 to SUA1, a value of SUB2 to SUB1 (data dump)
-performing the next acquisition
Therefore, the zero point of each sampling section is the signal acquired at the previous moment and is subjected to program operation, so that the real-time flow and the flow speed at the moment can be obtained, a large amount of storage space is also avoided, in addition, the sampling time interval is reasonably set, and the sampling time interval is as short as possible.
The specific equivalents of the sensors are KA and KB, respectively, and the equations for calculating the real-time flow rate QR and the real-time flow rate FR of a and B from the sensor signals a (n) and (B (n) are as follows:
QRA(n+1)＝(A(n+1)-A(n))*KA,FRA(n+1)＝QRA(n+1)/T(n+1)；
QRB(n+1)＝(B(n+1)-B(n))*KB,FRB(n+1)＝QRB(n+1)/T(n+1)；
along with the running of the program, the system can automatically execute the cyclic process of sampling, zero point refreshing and calculation, and the following results are obtained in sequence:
QRA(1)＝(A(1)-A(0))*KA，QRA(2)＝(A(2)-A(1))*KA，......QRA(n+1)＝(A(n+1)-A(N))*KA；
FRA(1)＝QRA(1)/T(1),FRA(2)＝QRA(2)/T(2),......FRA(n+1)＝QRA(n+1)/T(n+1)；
QRB(1)＝(B(1)-B(0))*KB，QRB(2)＝(B(2)-B(1))*KB，......QRB(n+1)＝(B(n+1)-B(N))*KB；
FRB(1)＝QRB(1)/T(1),FRB(2)＝QRB(2)/T(2),......FRB(n+1)＝QRB(n+1)/T(n+1)；
t is a program-defined sampling interval, and if the same time interval is used each time, T (1) · T (n + 1);
in this way we have real time flow and velocity at each defined moment, although the shorter and more accurate the interval set, the reasonable interval time needs to be set, suitably 1-2 seconds.
As for verifying the effectiveness of zero point refreshing, 4 segments (10 seconds for each segment) of short start-output-stop are set, and as a result, the system is completely detected, displayed and recorded, and the result of the data recording of the scheme is shown in fig. 3;
the detection system adopting zero point refreshing obtains 15 groups of data, the A/B ratio is finally obtained according to weighting calculation and is 100:52.23, and the difference between the key control index and the following index of manual detection is only 0.1%.
In contrast thereto:
current method 1-manual weighing to detect weight ratio (a density 1.33, B density 1.13), reduced volume ratio 100: 52.26;
Having shown and described the basic principles and principal features of the invention and advantages thereof, it will be apparent to those skilled in the art that the invention is not limited to the details of the foregoing exemplary embodiments, but is capable of other specific forms without departing from the spirit or essential characteristics thereof; the present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein, and any reference signs in the claims are not intended to be construed as limiting the claim concerned.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (3)
1. The utility model provides a real-time on-line measuring system of multicomponent volume ratio of fluid output process, includes positive displacement flow sensor, programmable controller PLC and memory module, its characterized in that: the output end of the volume flow sensor is connected with the input end of a Programmable Logic Controller (PLC) through a data line, and the PLC is electrically connected with a storage module through the data line;
the storage module comprises six common storage units, wherein the six common storage units are SUA1, SUA2, SDA, SUB1, SUB2 and SDB.
2. The system of claim 1, wherein the system is configured to perform real-time on-line detection of a multi-component volumetric ratio of a fluid output process, and further configured to: and at least two volume type flow sensors are connected to the programmable logic controller PLC.
3. The system of claim 1, wherein the system is configured to perform real-time on-line detection of a multi-component volumetric ratio of a fluid output process, and further configured to: the real-time online detection system for the multi-component volume ratio in the fluid output process further comprises a display, and the display is connected with the Programmable Logic Controller (PLC) through a data line.
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