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This is a schematic diagram of the evaporation heat exchange process. I would like to examine the evaporation performance under different circulation rates (return flow rate + incoming fluid flow rate). May I ask how the automatic control logic should be designed appropriately? Option 1: Manually adjust the pump speed via frequency control + set a liquid level interlock for the heat exchanger to control the discharge valve ; Option 2: Manually adjust the pump speed via frequency control + set interlock control for the return fluid valve based on the return fluid flow rate + set interlock control for the outlet fluid valve based on the heat exchanger fluid level ; Option 3: Set interlock control of pump speed based on the heat exchanger liquid level + set interlock control of the return fluid valve based on the return fluid flow rate ; Option 4: Control the liquid outlet valve based on (inflow – vapor output) + use interlock control of the reflux liquid valve by setting its flow rate + adjust the pump speed by summing the flow rates of the various branches ; Which option is more cost-effective and easier to implement? Please, experts, discuss this, or are there any better suggestions?
To control the evaporation process with cyclic reflux, we need to consider efficiency, stability, and operability. Each solution has a different design approach and is suitable for different scenarios. The following is an analysis of each option: 1. **Option 1**: The method of manually adjusting the pump speed and controlling the discharge valve through level interlock is relatively basic. The advantage of this approach is its simplicity of operation, but it lacks automated control, which may lead to response delays and low efficiency. 2. **Option 2**: Building on Option 1, it adds control over the flow rate of the return fluid, thereby improving the automation level and processing accuracy of the system. However, this requires more sensors and control devices to achieve precise flow control, resulting in relatively high costs. 3. **Option 3**: This option uses the liquid level to directly control the pump speed in a linked manner, while also regulating the flow rate of the return fluid. It enables more automated control, allowing it to adapt better to changes in the process and maintain stable operation of the system. This approach can adjust automatically to accommodate changes in input, thereby improving the system’s response speed and reliability. 4. **Option 4**: By monitoring all key parameters (such as liquid level, flow rate, etc.) and implementing comprehensive control, this approach offers the most thorough control and can effectively optimize the operational efficiency of the entire process. But its complexity and cost are also the highest. Taking into account cost-effectiveness, implementation difficulty, and control effectiveness, **Option 3** may be a more balanced choice. It controls the pump speed via a level signal and regulates the flow rate of the return fluid, enabling it to adapt automatically to changes during the production process while maintaining a certain level of control accuracy and system stability; moreover, its implementation is relatively straightforward and its cost is moderate. The specific choice of solution still requires detailed analysis and consideration based on actual production conditions, budget, and technical support. In practical applications, on-site testing and adjustments may also be necessary to achieve the optimal operating condition. .
Poster: Relying solely on process flow diagrams to determine the control logic is likely insufficient; more detailed process flow charts and explanations of process parameters are needed. It is necessary to know the acidity and alkalinity of the system as well as the impurity content. Your device is similar to a single-effect evaporator; the evaporation rate depends not only on the feed volume but also on the temperature and pressure of the material inside the heater. There should also be parameters related to the amount of heat source, such as steam pressure, flow rate, temperature, etc. In the common single-effect evaporation process, a forced circulation pump is typically used alone; the product is collected by installing an overflow hole at the liquid level of the evaporator, from which a pipe leads to the product tank (the evaporator is a tank placed above the heater). Yours is connected to the outlet of the circulation pump, and the liquid level is controlled by adjusting a valve, which adds an extra step. If the system contains acid or suspended solids, this valve becomes a vulnerable component. During use, the feed rate is adjusted via an inverter, and by controlling the temperature of the heat source as well as the system’s negative pressure, it is possible to control the concentration of the product after evaporation. Multi-effect evaporation involves balancing the liquid level based on the level in the evaporator, by using PID to adjust the frequency of the pump in series; it also includes overflow from one stage to the next due to the height difference. (In actual use, the level gauge also requires maintenance.) A process flow diagram for the low-temperature waste acid concentration process with double-effect evaporation has been provided; it can be used as a reference.
This post was last edited by pzhmotor on 2024-8-9 at 10:01. The goal is to examine the evaporation effects under different circulation rates (return flow + incoming flow). The circulation rate can be adjusted by changing the speed of the circulation pump; it is much higher than the incoming flow (outgoing flow), so adjusting the circulation rate is the main focus.
1. Can this be considered a falling film or single-effect external circulation evaporator? 2. If the inflow rate remains constant, only the changes caused by variations in the circulation rate are considered. Thus, it is possible to monitor the flow rate of the return pump, the changes in liquid level inside the evaporator, and the changes in the amount of evaporation and condensation. 3. Does the circulation rate change, while the heating conditions remain unchanged?