Solving a Problem with LPHW Radiator

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Discussion Overview

The discussion revolves around solving a problem related to an LPHW (Low-Pressure Hot Water) radiator, specifically focusing on deriving block diagrams that illustrate the relationships between control signals, LPHW flow rates, heat output, and room temperature. The scope includes technical explanations and mathematical reasoning related to control theory and thermal dynamics.

Discussion Character

  • Technical explanation
  • Mathematical reasoning
  • Debate/contested

Main Points Raised

  • One participant proposes a block diagram showing the relationship between the control signal and radiator heat output, suggesting a simple flow from the controller to the LPHW valve and then to heat output.
  • Another participant suggests adding a block for the first order transfer function in the first diagram and expresses uncertainty about how to approach the second diagram, noting the need for thermal resistance and temperature gradient information.
  • A participant expresses difficulty in deriving the transfer function, proposing an energy balance equation and presenting a formula involving the temperatures of the LPHW and room.
  • Another participant provides a more detailed equation for heat flow rate and discusses the relationship between heat transfer and the rate of change of radiator output, indicating a potential path to derive the transfer function through Laplace transforms.
  • A later reply references an external source that approximates the relationship between room air temperature and radiator output heat as a first order transfer function, suggesting it may contain useful information.
  • A final post inquires about any updates or further developments regarding the problem-solving efforts.

Areas of Agreement / Disagreement

Participants express varying levels of understanding and approaches to the problem, with no consensus reached on the correct derivation of the transfer function or the complete block diagrams. Multiple competing views and uncertainties remain throughout the discussion.

Contextual Notes

Participants mention assumptions such as no losses in heat transfer and the need for information on thermal mass, indicating limitations in their current understanding and the complexity of the dynamic situation being analyzed.

jami8337
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I am trying to solve a problem regarding an LPHW radiator, of which the heat output is controlled by adjusting the LPHW flow rate. The relationship between the flow rate and the radiator output can be approximated by a first order transfer function with a time constant of 1 minute. The heat output is adjusted by a control signal directed to a final control device that determines the LPHW flow rate.

I now need to draw two open loop block diagrams The first showing the relationship between the control signal and the radiator heat output. The second of the relationship between the heat output and the room temperature.

I am at a loss on what to do for the first diagram, however it may just be me overthinking it. Would it simply be:

i ----> Controller -----> LPHW Valve -------> Heat Output

Any insight would be greatly appreciated

Thanks
 
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I think you probably need to add a block showing the first order transfer function. Something like..

I---> Controller -> LPHW Valve --> LPHW Flow rate ---> Transfer function ----> Heat Output

Replace "Transfer function" with the actual equation.

Not sure how to do the second one. I'm familiar with steady state heat loss calculations (you need thing like the thermal resistance of the walls and the temperature gradient across them) but your question suggest a dynamic situation (for which you probably need information on the thermal mass?).

Sorry that's the best I can manage.
 
Thanks for your help, I think i can draw both the block diagrams, but I am hitting a wall when having to derive the transfer function for the first one. This would be based on the energy balance equation i believe, but i am a bit lost trying to derive that. I have come up with:

(TW-Ti)/R

Where Tw is the temperature of the LPHW, and Ti is the room temp...
 
Okay here is what i have come up with:

Temperature LPHW = θL
Temperature Output = θO
Heat Flow rate = Q

Q=(θLO)/R

Assuming no losses. The heat transferred from the LPHW alone determines the 'Radiator output' to the room. Therefore the rate of heat transfer will determine the rate of change of the radiator output, hence:

O/dt = Q/C (C = Capacitance)

Then:

O/dt = (θLO)/RC

I can then rearrange this and take a laplace transform to give me the transfer function. Does this sound like the right sort of track to be on?

Thanks!
 
Whats up? Any further news regarding these efforts?
 

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