QUESTION: I am designing a small organic Rankine cycle unit to produce about 1.2 kilowatts of electrical power. The working fluid is refrigerant R-134a. The heat source is a tank of solar heated water at about 150 °F. and the heat sink is the basin water in a swamp cooler or small cooling tower that will be at about 65 °F to 75 °F.
A copper coil immersed in the solar-heated water tank will serve as the boiler, and the condenser will either be a brazed plate heat exchanger or a copper coil immersed in the cooling tower or swamp cooler basin.
Heat-pump-assisted 1.2 KW solar electricity generator for a private
An automotive scroll compressor will be converted to serve as the expander by removing the compressor’s check valve. The turbine will be shaft coupled to an alternator that will produce electricity. The pump will probably be a DC- electric motor-driven gear pump.
I am aware that turbines are typically speed controlled, and boilers are usually pressure controlled.
My question is how do I control this system? I have thought of two approaches:
- The boiler could be fitted with a pressure transducer that would serve as an input to a PID process controller. The PID controller would issue a 4-20 mA command signal to a device that would convert the signal to a pulse width modulated power output that would vary the gear pump’s motor speed to maintain constant boiler pressure.
- The shaft of the scroll expander could be fitted with a speed sensor that serves as the input to a PID controller. The PID controller would issue a 4-20 mA command signal to a device that would convert the 4-20 mA command signal to a pulse width modulated power output that would vary the gear pump’s motor speed to maintain constant expander speed.
In the first case, the boiler pressure would be controlled, but the expander speed would be uncontrolled. In the second case, the expander speed would be controlled, but the boiler pressure would be uncontrolled.
I’m not very comfortable with either case. Can you suggest the proper control solution?
Answer: Einstein said, “The future cannot be guided by the thinking of the past.” This also holds true for our profession. The control requirement of renewable energy processes requires new control strategies. So, while your plan to make your own electricity from solar source is good, I would not use either of your schemes, but would do the following.
The main variable in your process is the insolation. The changes in insolation are reflected by the temperature of the solar hot water. Therefore, a simple control scheme (Figure 1) is to look at both the temperature difference between the solar collector (T1) and the solar water tank (T2) and start the water pump (P1) when T1 > T2 by over, say, 20 °C and stop it when it drops to 10 °C using a differential thermostat ΔTC-1.
The same holds true for the Rankine cycle refrigerant pump (P2). Because the condenser (swamp) temperature is more or less constant, I would not bother with detecting the ΔT and would just look at the boiler (water tank – T2) temperature and keep P2 running whenever the T2 temperature is above 60 °C (140 °F), bringing P2 to full speed as T2 reaches, say 70 °C, controlled by TC-2.
If you want to maximize the efficiency of the system, you can do better than the above, but such an approach costs more, and I do not think it is justified. In that case, the measured variable would be the ΔT between the boiler and condenser waters (both variables). You would prepare a three-dimensional plot, where the coordinates are ΔT, refrigerant flow and net electricity production. The net electricity produced is the difference between the power generated minus pumping power invested. This three-dimensional surface will have a maximum value for each ΔT. You would read the flow corresponding to that maximum and set the pump speed to match it. With a large system (a geothermal power plant using ground water or a lake as its heat source), this might make sense. You might get another 10% more power, but with your system (where the basin temperature is relatively constant and the system is small),the effort required does not pay.
QUESTION: How do you select a suitable volume booster for a cylinder actuator + positioner for double-acting/ spring-return cylinder actuators? Is it possible to have an example of the selection process?
Answer: The vendor should know what is really needed. If this is a new installation, I would purchase the system assembled and tested. If a retrofit, I would ask the vendor representative to make a recommendation, but use common sense to check it. In any event, be certain that the air supply is adequate. If a large actuator is involved, the compressed air source can easily limit the actuator speed. I have seen large air tanks installed near large valves in critical service, in this case, a large air compressor anti-surge valve.
Answer: In my experience, inserting a booster between a positioner and valve actuator introduces dead band into the loop, resulting in a limit cycle when controlling pressure and liquid level. I do not recommend this practice.