基于ControlLogix5550 PLC的锅炉水位控制系统毕业论文外文翻译.docx

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1、Boiler level control system based on ControlLogix5550 PLCAbstract-This paper is a research design based on EFPT process control device. In the design, actual industry field has been simulated and corresponding modeling has been carried on for the boiler level system. Then the appropriate PID paramet

2、er has been sorted out and ControlLogia5550PLC has been used to control the entire boiler level system.At last, a corresponding control interface has been established and the boiler level has been under a safe and accurate controlKeywords：EFPT，PID，Modeling，Boiler level;1 IntroductionThe task of the

3、industrial boiler level control is to maintain a dynamic balance by controlling the water flow and evaporation, so that the drum level can be maintained in the technological level, which is a necessity for ensuring safe operation and also one of the main indicators of the boilers normal operation. W

4、ater level which is too high will affect the effect of the steam-water separation, but too low it is will break ring cycle or even cause boiler explosion. To ensure a safe and efficient production, the boiler level must be strictly controlled in maintaining constant or changing only according to a c

5、ertain rule. Using Logix5550 PLC with analogy I/O modules, launched by Rockwell Automation Company as controllers, and EFPT process control experimental device as control object, this system have brought the boiler water level under an accurate control in a mini boiler system with sensors and actuat

6、ors that used in industrial production.Fig. 1 Boiler level setting value adjustment system2 System Overview This system is composed of an EFPT process control device, an inverter, a Logix5550 PLC and a computer. EFPT process control device is a simulated heating and water supply and drainage system

7、for a micro-small boiler. It realizes process control in a mini boiler system with sensors and actuators used in industrial production. The actuator includes not only measuring appliance, but also AC inverter, heating controller, heater and so on. The system simulates industry scene through a mini-b

8、oiler heating, water supply and drainage system, which is reliable and visual. In the design, boiler Level was selected as the controlled variable. The controlled object is composed of the water trough, the force pump, the boiler and the pipe-line valve. Micro Master 6SE9214-ODA40 inverter is taken

9、as the actuator and the boiler level is controlled by Logix5550. Configuration software RSView32 and touch screen PanelView1000 are combined to realize the real-time monitoring. In the design, a simple design of single-loop boiler liquid level value adjustment is selected for the study. The composit

10、ion of the system is shown in Fig. 1. In the design, the inverter as an actuator directly receives PLC analogy I/O port output, and converters into frequency of inverter so as to drive the 3-phase motor in the lift pump, change the inlet, and adjust the boiler level to the dynamic balance at last. A

11、nd the configuration software is used to design monitoring picture to realize the computer and the touch screen to the boiler level long-distance and the scene monitoring. 1. Pump started, pid controller pressure transmitter to the control point to provide the pressure signal, when the pressure poin

12、t is not equal to set value, pid controller by adjusting the inverter output frequency to change the pump speed to regulate the pipeline pressure constitutes a closed-loop feedback control system, water pressure regulator so that users timely, small fluctuations in results. And in the process contro

13、l system designed to take full account of the principle of load balancing, to take first-in-first out strategy of lining up, the way the implementation of the rotating frequency to ensure that the basic balance of the water usage. 1 Frequency Control Constant Pressure Water Supply Principle Frequenc

14、y Control Constant Pressure Water Supply System by the programmable logic controller (plc), converter (built-pid), pressure transmitter, low-voltage electrical and pump components, such as Figure 1. Map m1 m3 for water pump motors, p1 p3 for pumps, km1 km6 for motor starting and stopping each of the

15、 AC contactor switch. Basic working principle of the system: by the plc a signal to the inverter to control the water cycle work, when the large volume of water consumed by the plc control of all water line installed in the outlet pipe of the pressure transmitter, pressure standard signals into dc 0

16、 v 10 v into the analog signal converter with pid regulator, pressure settings and pressure feedback values after the implementation of pid calculated values of the output of a frequency converter to set the value for the pump by the inverter to provide variable frequency electrical power to realize

17、 stepless speed regulation of electric pumps to regulate the exit of the water supply pipe network pressure, constant pressure water supply to achieve the purpose. Pressure feedback signal in order to ensure an accurate value, yet the value of feedback signal to set the filter time constant. The sco

18、pe of the power converter, Figure 1 can increase the number of the motor to achieve a multi-trailers, Optimization of the program.3 Establishing Mathematics model for the charged object One of the main tasks of establishing control system mathematical model is to determine the mathematical model of

19、the controlled object. Generally, there are two kinds of basic methods for establishing process control mathematical model: mechanism analysis and experimental method. However, for controlled object whose structure and internal process is very complex, it is very difficult to determine the object ju

20、st by its own internal physical process and to solve out the differential equations systematically. Besides, considering the nonlinear factor, mechanism analysis used some approximation and hypothesis for mathematical deduction. Although these approximation and assumptions have practical basis, but

21、not fully reflect actual situation, and even cause incalculable effects. Therefore, in this design, the experimental method is chosen to establish a mathematical model for controlled object. This kind of modeling is based on the input and output in the actual production process, that is to say, esta

22、blishing mathematical model for the controlled object through process identification and parameter estimation. In this design, step response curve method is used to identify mathematical models of the process. A 20Hz step disturbance input signal is applied to the charged object, and the response cu

23、rve of the output that changes with time can be mapped. After the analysis, the transfer function of the controlled object can be defined. In the process of experiment, the object was conducted several tests. Using RSLogix5000 trend monitoring function curve, more than 10 charged object step respons

24、e curve have been recorded. To all the parameters for average, steady time: ts821.525s, steady value: h()=58.5, peak time: tp=394.4s overshoot: a%29%. According to the theoretical analysis, the controlled object is the most likely second-order object.However, the difference is very apparent between

25、the ideal second-order controlled object step response curve and the actual curves. So the ideal curve cant response to its actual characteristics. It is inferred that the controlled object may be the second-order controlled object that includes zero. The try and error method and MATLAB simulation t

26、ools are used to get a curve whose parameters are close to the average dynamic parameters of the controlled objects response curve. It is shown in Fig. 2. Some adjustments can be made according to the following rules: 1) When the zero is closer to the imaginary axis, settling time will be longer and

27、 the overshoot will be bigger and peak time will be smaller. With the zero closing to the imaginary axis, the effect is more obvious. 2) The effect which the closed loop dominant apices have on dynamic performance is increasing the peak time, reducing the overshoot and adjusting time. Nonparametric

28、model is used to describe the controlled object. In other words, step response curve which approximately describe the controlled object is used because of the controlled objects complexity and uncertainty. To a constant water supply, landing in the water pressure to increase the inverter output freq

29、uency, when the maximum frequency converter and a constant pressure pump can not meet the requirements, while running the pump frequency to switch to the running frequency, At the same time need to start a second frequency or third pump until the water supply to meet the requirements. Need to determ

30、ine criteria for the launch of a new water pump is the inverter output frequency is set to reach the upper limit. In order to determine the frequency of the inverter limits the accuracy of least squares by chance should be the frequency of the frequency of fluctuations in the ceiling from the situat

31、ion. Inverter control motor pumps are activated each time the soft-start, and requires the use of water pumps must turn to serve as a continuous variable frequency pump operation shall not exceed 3 h, each time when the need to launch a new water pump, the pump will run from the existing removal of

32、the inverter, and replace the power-frequency operation, reset the inverter and run the pump for a new start. Three pumps to control the duty cycle is the use of pump No. 1 way to achieve (to 3 in the plus 1 equal to zero), or combined with the total number of pump pump pump rotation to achieve its

33、work.4 The installation of controller parameter4.1 The selection of control algorithmAfter establishing the approximate mathematical model of the controlled object, a complete feedback control system can be formed to improve the performance of the open-loop control system. PID is an ideal control la

34、w in that integral is introduced basing on the proportion, which can eliminate the residual error, plus the derivative action, which can also improve the stability of the system. According to the characteristics of the controlled object and laboratory conditions, a single-loop feedback control loop

35、for the controlled object is established, and PID algorithm is used to realize boiler level control. The schematic diagram of level control is shown in Fig. 3. Open the outlet valve to a certain degree, and make the hydraulic discharge invariable. Comparing the process variables of the water level i

36、n feedback with the given volume, the deviation can be obtained. PID instruction does PID operation on the deviation, and the results is a control variable, so the frequency of the inverter can be changed to control the rotate speed of the pump. If the liquid level is on the high side, the results m

37、ake the control variable smaller, andreduce the rate of inflow, make liquid level lower; if the level is on the low side, the results make the control variable larger, and increase the rate of inflow, make liquid level higher.4.2 The Parameter Tuning of PID Because the transfer function of the contr

38、olled object includes a zero second-order link, the computation work load is quite big regardless of using the root-locus method or the frequency characteristic law among theory methods when tuning PID parameter. And the process mathematical model can only reflect dynamic parameter approximately, so

39、 the reliability of the parameter value which is obtained by the theoretical calculation is not very accurate and it will be adjusted constantly in the scene. Therefore, engineering parameter tuning is chosen to seek the PID parameter in the design. The common method of engineering tuning are dynami

40、c characteristic parameters, the stable boundary law, the decay curve law and field experience setting method, etc. In the process of PID parameters, the 4:1 decay curve law isadopted. The steps are: 1) In the closed system, regulators integral time is set the largest (Ti) and differential time Td i

41、s set zero (Td=0). The proportion is taken the great value to perform the given value perturbation experiment repeatedly, and the proportion is reduced gradually until the record curve presents up to 4:1 weaken. Then the proportion is called 4:1 weaken proportion s sand the distances between two nei

42、ghboring wave ridges are called 4:1 damped cycle Ts. In the experiment, the level quantitative test is set for the 200mm, and then the system response curve is obtained and reorganized 4:1 decay curve (thick red line is shown in Fig. 4 Thus measuring: s8，Ts2.2; 2) According to the following formula,

43、 each parameter of the regulators is =0.8, s6.4; Ti=0.3, Ts6.6; Td=0.1, Ts2.2 3) According to these results, regulator parameters are set. Then the dynamic process of system is observed and the parameters are made adjustment to determine the optimum parameters.5 Monitoring Design Frequency according

44、 to the principle of constant pressure water supply system the design water level control system of the water tower block diagram shown in Figure 2, the city water network eq with the water level controller to control the injection valve yv1, as long as the water level below the high water mark, the

45、n to the pool water automatically. Pool of high / low water level signal directly to the plc, as a high / low level alarm. In order to ensure continuity of supply, the water level of the smaller distance between the upper and lower limits. Domestic water and fire water pump three shared 3, usually y

46、v2 solenoid valve in a state of loss, the closure of the fire pipe network, when a fire occurs, the solenoid valve was yv2 electricity, water distribution network with the closure of life, three water pumps for fire use, and maintain high-pressure fire water value. After the lifting of the fire, thr

47、ee use domestic water pump replaced and the cycle of operation, to maintain constant low water value. Each pump motor can run frequency, and frequency can be run. When the small volume of water consumed, a water pump under the control of the converter stable operation of large quantities of water to

48、 the pump when running at full speed there is no guarantee that the pressure on network stability, plc pressure given the lower limit of the inverter signal and high-speed signal at the same time plc was detected, plc automatically work in the original state of the pump frequency into frequency oper

49、ation, in order to maintain the continuity of pressure at the same time use the next pump put into operation after start-up converter in order to increase the supply pipe network pressure of water to ensure stability; if running two pumps can not meet the requirements of the pressure, the frequency of work will be followed by a sta