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How to simulate propane (r-290) heat pump heating a hydronic loop

A single-stage vapor-compression heat pump delivering heat to a space-heating water loop — the same cycle as a refrigerator, read from the hot end. Propane evaporates at 4.7 atm (273 K, an air- or ground-source evaporator at 0 °C), is compressed to 21 atm (condensing at 333 K, 60 °C) and condenses against the heating water in a real two-sided exchanger, so the delivered heat is a water stream you can read: 40 °C return warmed to 59 °C. A small makeup feed and purge close the refrigerant mass balance around the recycle, as in the refrigeration examples. Two numbers define the machine: 80 kW delivered for 28 kW of compressor work, a heating COP of 2.9 — 52% of the Carnot limit for this 60 K lift, which is where a real R-290 unit sits. Read COP on the flowsheet as the user variable cop_heating, or sweep the condensing pressure: from 18 to 27 atm the COP falls 3.2 → 2.6 as the lift grows, the trade every heat pump makes between water temperature and electricity. Honest scope: the compressor is a fixed isentropic efficiency, the condenser outlet is a specified subcooling, and there is no defrost, part-load or refrigerant-charge model. Below ~18 atm the specified 326 K condenser outlet sits above saturation and the cycle stops condensing — the sweep starts where the physics does.

Makeup
MIX
COMP
Heating Water
hot
cold
hot
cold
Q out
COND
Valve
EVAP
Split
Purge
HOT Water
  1. 1
    Open the ready-made model

    Open the "Propane (R-290) heat pump heating a hydronic loop" model in the MaximaLabs workspace — no install, no license. It loads live on the canvas, ready to edit and run.

  2. 2
    Confirm the thermodynamics

    This process is modeled with the COOLPROP property package over propane, water — already selected, so the phase equilibrium and enthalpy are physically consistent from the first run.

  3. 3
    Review the flowsheet

    The flowsheet chains MIX, COMP, COND, Valve, EVAP, Split. Every block is a real, solvable unit op you can reconfigure on the canvas.

  4. 4
    Run the simulation

    Click Run. The deterministic solver converges the material and energy balances (recycles included) and fills the live stream table — the AI never invents a number.

  5. 5
    Read the results and iterate

    Inspect the converged streams, tweak a spec, and re-run — or ask the AI copilot to explain a result or diagnose a failed solve in plain English.

What you'll build
Thermodynamics
COOLPROP
Components
propane, water
Unit operations
MIXCOMPCONDValveEVAPSplit
Open this model in the workspace

Opens live on the canvas — free, no install.

Explore the model & flowsheet

Frequently asked questions

What does the Propane (R-290) heat pump heating a hydronic loop model simulate?
A single-stage vapor-compression heat pump delivering heat to a space-heating water loop — the same cycle as a refrigerator, read from the hot end. Propane evaporates at 4.7 atm (273 K, an air- or ground-source evaporator at 0 °C), is compressed to 21 atm (condensing at 333 K, 60 °C) and condenses against the heating water in a real two-sided exchanger, so the delivered heat is a water stream you can read: 40 °C return warmed to 59 °C. A small makeup feed and purge close the refrigerant mass balance around the recycle, as in the refrigeration examples. Two numbers define the machine: 80 kW delivered for 28 kW of compressor work, a heating COP of 2.9 — 52% of the Carnot limit for this 60 K lift, which is where a real R-290 unit sits. Read COP on the flowsheet as the user variable cop_heating, or sweep the condensing pressure: from 18 to 27 atm the COP falls 3.2 → 2.6 as the lift grows, the trade every heat pump makes between water temperature and electricity. Honest scope: the compressor is a fixed isentropic efficiency, the condenser outlet is a specified subcooling, and there is no defrost, part-load or refrigerant-charge model. Below ~18 atm the specified 326 K condenser outlet sits above saturation and the cycle stops condensing — the sweep starts where the physics does.
Which thermodynamic method does it use?
The COOLPROP property package, over propane, water — already selected. You can switch the method on the canvas before running.
Which unit operations are in the flowsheet?
It chains MIX, COMP, COND, Valve, EVAP, Split. Every block is a real, solvable unit operation you can reconfigure, add to, or remove.
Do I need to install software or buy a license?
No. Propane (R-290) heat pump heating a hydronic loop runs entirely in your browser on MaximaLabs — free, no install, no license. Open the model to load it live and run the deterministic solver.

More guides like this

Reference model (ChemSep)

Propane refrigeration cycle

A single-stage vapor-compression refrigeration loop: propane vapor is compressed, condensed to subcooled liquid, throttled through a valve, and superheated back to vapor in the evaporator before recycling — a small makeup feed and purge close the mass balance (inspired by ChemSep's Refrigeration_* reference cases).

Reference model (ChemSep)

Ammonia refrigeration cycle

A single-stage vapor-compression refrigeration loop using ammonia — the classic industrial (rather than HFC) refrigerant — condensed to subcooled liquid, throttled through a valve, and superheated back to vapor in the evaporator before recycling (inspired by ChemSep's Refrigeration_Ammonia-30C reference case).

Amarillo, Texas, USA

Helium liquefaction (Linde-Hampson cycle)

A Joule-Thomson liquefaction loop: helium is compressed, aftercooled, precooled well below its ~40-51 K JT-inversion temperature, then throttled through a valve into a flash drum that draws off liquid helium while the cold vapor recycles back to the compressor suction — the same JT-cycle physics as the platform's LNG/refrigeration loops, run on a fluid whose inversion curve makes precooling mandatory before the throttle can cool it at all.

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LOHC hydrogen release (methylcyclohexane dehydrogenation)

A liquid organic hydrogen carrier (LOHC) power train: methylcyclohexane (MCH) is preheated and catalytically dehydrogenated (MCH → toluene + 3H2, endothermic, equilibrium-limited to ~90% single-pass conversion) to release hydrogen for downstream power generation. A flash drum separates the H₂-rich gas from the liquid; a distillation column then recovers the unreacted MCH overhead and recycles it to the reactor feed, closing a real tight liquid recycle loop, while spent toluene leaves the bottoms (to be re-hydrogenated back to MCH off-site, closing the supply-chain loop — out of scope for this dehydrogenation-side flowsheet). Screening-fidelity note: MCH and toluene are genuinely close-boiling (relative volatility ~1.4 under this thermo package at column conditions), so the recycle carries real toluene along with the recovered MCH rather than a sharp cut — a production column would use more stages to purify it further; this shows the recycle topology and its convergence, not an optimized column design.

Reference model

Recycle loop

A mixer/heater/splitter loop with a tear stream — exercises Wegstein recycle convergence.

Propylene splitter, Mont Belvieu, Texas, USA

Vapor re-compression propane/propylene splitter

Propylene/propane splitters have a notoriously low relative volatility (~1.1-1.15), so they run at high reflux and benefit from heat pumping: the overhead vapor is compressed and used to reboil the same column at a lower operating pressure (here 12 bar vs. a conventional ~20 bar), cutting the compressor shell cost (Christopher et al., Ind. Eng. Chem. Res. 56, 14557, 2017). The reboiler heat-integration loop itself is not modeled here (that would need a recycle-coupled duty match) — this shows the column plus the overhead compression/condensing train, a bounded simplification.

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