TXV Charging Curve Quick Reference

TXV Charging Curve Overview

  • The chart used is the TXV charging curve; axes: left vertical = refrigerant line lift (ft), bottom axis = total refrigerant line length (ft). Middle shows three curves: lower, middle, upper.
  • Rule: if the operating point lands below the curves, you need to add refrigerant; if it lands above the curves, you need to remove refrigerant.

Curve Selection Criteria

  • Step 1: Measure the liquid line temperature. Example: TextLL=100v0 ∘F.T_{ ext{LL}} = 100^{\\v0}\mathrm{\,\circ F}.
  • Step 2: Determine line length and vertical lift:
    • Total line length: distance from condenser to evaporator.
    • Vertical lift: is the evaporator higher than the condenser? quantify height in feet.
    • If indoor section is above condenser, use the given lift value.
  • Step 3: Plot the intersection of (line length, lift) on the chart to choose the curve: lower, middle, or upper.
  • Guidance: for long line sets or large vertical lift, use the upper curve to account for pressure drop and require more subcooling.
  • Practical purpose: manufacturers design these curves to ensure proper charge and better system performance.

TXV Curve Application: Pressure-Temperature Plot

  • After selecting the curve, plot the pressure and temperature on the TXV curve:
    • LLT: TextLLT_{ ext{LL}} on the liquid line axis.
    • High-side pressure: PextHSP_{ ext{HS}} (psig).
  • If the intersection lands on the chosen curve (e.g., middle curve), the charge is considered correct.

Example: R-22 System

  • Given: T<em>extLL=100∘F,P</em>extHS=233 psig.T<em>{ ext{LL}} = 100^{\circ}\mathrm{F},\quad P</em>{ ext{HS}} = 233\ \mathrm{psig}.
  • The intersection with the middle curve aligns with the middle curve, indicating the charge is appropriate.
  • Read the corresponding saturation temperature: on the chart for R-22, around the point corresponding to this pressure, Textsat≈112∘FT_{ ext{sat}} \approx 112^{\circ}\mathrm{F}.
  • Subcooling calculation (per example): ΔT<em>sub=T</em>extsat−TextLL≈112∘F−100∘F=12∘F.\Delta T<em>{\text{sub}} = T</em>{ ext{sat}} - T_{ ext{LL}} \approx 112^{\circ}\mathrm{F} - 100^{\circ}\mathrm{F} = 12^{\circ}\mathrm{F}.
  • So, using the middle curve yields about 12∘F12^{\circ}\mathrm{F} of subcooling.

Subcooling and Reading Charts

  • Subcooling is the difference between the saturated liquid temperature at the high-side pressure and the actual liquid line temperature after the coil: ΔT<em>sub=T</em>extsat−TextLL.\Delta T<em>{\text{sub}} = T</em>{ ext{sat}} - T_{ ext{LL}}.
  • Read and compare against the P-T chart to verify the curve selection and the implied subcooling.
  • Important: each manufacturer may format charts differently; the core skills are accurate measurements and applying them to the chart correctly.

Key Takeaways

  • Use the line length and lift to choose the appropriate TXV curve (lower/middle/upper).
  • If the plotted point is below the curves, add refrigerant; if above, remove refrigerant.
  • Verify with the P-T chart: ensure the LLT and HS pressure intersect the correct curve for the expected subcooling.
  • Read charts and tables carefully; manufacturer variations require solid measurement and interpretation skills.