Air Density Calculator
Calculate air density from pressure, temperature, and humidity using the ideal gas law. Includes altitude reference table and moist air corrections.
Calculate heat exchanger effectiveness using the ε-NTU method for counter-flow, parallel-flow, shell-and-tube, and crossflow configurations.
| NTU | Counter (%) | Parallel (%) | Crossflow (%) |
|---|---|---|---|
| 0.5 | 36.2 | 35.2 | 33.4 |
| 1 | 56.5 | 51.8 | 54.5 |
| 1.5 | 69.1 | 59.6 | 68.5 |
| 2 | 77.5 | 63.3 | 78.0 |
| 2.5 | 83.3 | 65.1 | 84.6 |
| 3 | 87.4 | 65.9 | 89.1 |
| 4 | 92.7 | 66.5 | 94.5 |
| 5 | 95.7 | 66.6 | 97.2 |
| 6 | 97.4 | 66.7 | 98.6 |
| 8 | 99.1 | 66.7 | 99.6 |
The effectiveness-NTU (ε-NTU) calculator determines heat exchanger performance without requiring outlet temperatures as inputs. This method is the standard approach when only inlet temperatures and flow rates are known, making it the preferred technique in preliminary design and rating problems.
The method relates heat exchanger effectiveness (ε) to the Number of Transfer Units (NTU = UA/Cmin) and the capacity ratio (Cr = Cmin/Cmax). Effectiveness represents the fraction of maximum possible heat transfer actually achieved. Different flow configurations — counter-flow, parallel-flow, crossflow, and shell-and-tube — yield different ε-NTU relationships, with counter-flow always providing the highest effectiveness for a given NTU.
This calculator handles all standard configurations, computes outlet temperatures, and provides comparison tables so engineers can evaluate design trade-offs. Whether you are sizing a new heat exchanger or rating an existing one, the ε-NTU method delivers quick, reliable answers for thermal system design. This context keeps the calculation practical and easier to apply in real scenarios.
The ε-NTU method is the backbone of heat exchanger analysis in HVAC, chemical processing, power generation, and automotive thermal management. This calculator saves engineers from manual chart lookups by computing effectiveness for four configurations and providing comparison tables for design trade-offs. It helps reduce avoidable mistakes and keeps results aligned with practical workflow expectations.
Counter-flow: ε = (1 − exp(−NTU·(1−Cr))) / (1 − Cr·exp(−NTU·(1−Cr))). Parallel-flow: ε = (1 − exp(−NTU·(1+Cr))) / (1+Cr). For Cr=0: ε = 1 − exp(−NTU). Q = ε·Cmin·(Thi − Tci). NTU = UA/Cmin.Result: 80.5% effectiveness, 281.6 kW heat transfer
With NTU=2 and Cr=0.5 in counter-flow: ε = (1−e^(−2×0.5))/(1−0.5×e^(−2×0.5)) ≈ 0.805 (80.5%). Q = 0.805 × 5000 × 70 = 281,750 W.
Calculate heat exchanger effectiveness using the ε-NTU method for counter-flow, parallel-flow, shell-and-tube, and crossflow configurations. Use it when you need a repeatable calculation in the physics / general category and want the setup, result, and supporting values kept together. This is especially helpful when small input changes, unit choices, or rounding decisions can change the final number.
Start by confirming that the inputs match the formula shown on the page. Then compare the main output with the worked example and any secondary values shown by the calculator. If the result will be used in another calculation, keep extra precision until the final step and record the assumptions beside the number.
Treat the result as a calculation aid rather than a substitute for context. For schoolwork, include the formula and substitution steps. For planning, technical, financial, or health-related decisions, verify important numbers against primary records, current rules, or a qualified professional before acting on them.
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NTU (Number of Transfer Units) is a dimensionless parameter equal to UA/Cmin, where U is the overall heat transfer coefficient, A is the area, and Cmin is the smaller heat capacity rate. Higher NTU means more heat transfer area relative to fluid capacity.
Use ε-NTU when outlet temperatures are unknown (rating and design problems). Use LMTD when all four temperatures are known and you need to determine the required area.
In counter-flow, the temperature difference between fluids is more uniform along the length, maintaining a higher driving force throughout. Parallel-flow suffers from a decreasing temperature difference toward the outlet.
Cr = 0 occurs when one fluid undergoes a phase change (condenser or evaporator), meaning its effective heat capacity is infinite. The ε-NTU relation simplifies to ε = 1 − e^(−NTU).
Theoretically, 100% effectiveness requires infinite NTU (infinite area). In practice, 80–95% effectiveness is typical for well-designed counter-flow exchangers.
If you know the required ε and Cr, you can find the needed NTU from the charts, then compute the required area A = NTU × Cmin / U.
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