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Calorimeter calibration establishes the response of the actual measurement assembly to a known energy input. It determines a participating heat capacity, not just the empty vessel's mass. For an electrical calibration with an immersed resistor, measure voltage $V(t)$ across that resistor and electric current $I(t)$ through it. If that electrical work is deposited inside the chosen boundary, its input isFor a covered receiver at constant pressure, $C_{\mathrm{eff}}$ describes enthalpy storage; for a rigid fixed-volume assembly, use the matching heat capacity at constant volume. Negligible endpoint mechanical storage and no escaping material are assumed. Thus $E_{\mathrm{el}}/(T_1-T_0)$ overestimates $C_{\mathrm{eff}}$ if outward loss is ignored. Account for lead losses outside the boundary and maintain the same water charge and immersed hardware in calibration and sample runs.

An alternative calibration mixes known hot and cold water portions. With the vessel initially at the cold portion's temperature $T_c$, the mixing calorimetry balance givesThe previous synthetic water example returns $100\mathrm{J}{\mathrm{K}}^{-1}$. The sign matters: attributing room losses to the vessel makes this estimate too large. With both $C_{\mathrm{cal}}$ and the loss unknown, one final temperature supplies only one equation; separate cooling information or controlled independent runs are needed.

A calorimeter heat-loss correction can make the electrical balance quantitative. For a second synthetic example, stipulate $0.100\mathrm{kg}$ of water with $c_w=4180\mathrm{J}\mathrm{k}{\mathrm{g}}^{-1}{\mathrm{K}}^{-1}$ and immersed hardware with $C_{\mathrm{cal}}=82\mathrm{J}{\mathrm{K}}^{-1}$, so $C_{\mathrm{eff}}=500\mathrm{J}{\mathrm{K}}^{-1}$. Supply $10\mathrm{W}$ for $300\mathrm{s}$, starting at a room temperature of $20{}^{\circ }\mathrm{C}$, with loss coefficient $G=1\mathrm{W}{\mathrm{K}}^{-1}$. The model below gives $T_1\approx 24.512{}^{\circ }\mathrm{C}$, storage $2255.942\mathrm{J}$ and outward loss $744.058\mathrm{J}$. The uncorrected ratio gives about $665\mathrm{J}{\mathrm{K}}^{-1}$; subtracting the loss recovers $500\mathrm{J}{\mathrm{K}}^{-1}$.

A calorimeter heat-loss correction estimates the signed heat exchanged with the room during the measurement. Under Newton's law of cooling, a constant room temperature $T_a$ and a single representative assembly temperature $T$ give the modelHere $P(t)$ is deposited input power, and $G$ is the apparatus loss coefficient in $\mathrm{W}{\mathrm{K}}^{-1}$. After input ceases, the temperature excess shows exponential decay with time constant $\tau =C_{\mathrm{eff}}/G$:A cooling trace determines the ratio $G/C_{\mathrm{eff}}$, not the two factors separately. Combining the cooling trace with a known electrical energy input supplies the missing information. For constant input $P_0$, starting at $T_a$, the heating solution is $T(t)-T_a=(P_0/G)(1-e^{-t/\tau })$; these solutions generate the calibration figure.

For mixing calorimetry, infer cooling behavior only after the sample, water and vessel approach a common temperature. Applying a single-body cooling model while the sample remains much hotter than the water can misestimate the earlier loss. The Toronto handout's area correction assumes the same loss mechanism represents both the mixing interval and subsequent cooling.^[ref] A backward extrapolation to the transfer time is therefore a model-dependent estimate, not the ultimate equilibrium with the room. Extend the model or report a limitation if sensor delay, substantial temperature gradients, changing room temperature, or escaping material invalidate that assumption. In particular, the relevant $C_{\mathrm{eff}}$ after adding a sample includes its heat capacity; an empty-receiver cooling rate need not apply to the loaded receiver.

Calorimetry measures heat transfers. A calorimeter, a calibrated heat capacity and an accounting of unwanted heat transfer connect an observed temperature change to an energy balance, as in heat-engine calorimetry and heat-pump calorimetry.

The central idea is to measure a response that is easier to observe than the transfer itself: a known heat capacity turns a temperature change into an energy estimate. Mixing calorimetry can determine an unknown specific heat capacity, while a chemical reaction can be studied by measuring the response of its surroundings. The useful observable is a change in temperature, together with a stated thermodynamic system boundary; a hot object does not contain a separately conserved store of heat.

For a closed system with unchanged bulk kinetic energy and potential energy, let $Q_{\mathrm{in}}$ be net inward heat and $W_{\mathrm{on}}$ net inward work. The first law of thermodynamics givesIf the boundary includes a hot sample, receiving water and the participating vessel, their mutual heat transfer is internal. With no external input, the total storage change is minus the signed outward heat leakage, not the positive amount transferred from sample to water. A calorimeter calibration with an immersed resistor instead supplies electrical work across this boundary; Joule heating converts it into internal energy. Choosing only the receiving water as the boundary changes which transfers count as external.

The mechanical constraint decides which storage quantity the readout represents. For a closed system at fixed volume, with no other work, $Q_V=\Delta U$. At constant external pressure, with only expansion work $p\Delta V$, $Q_p=\Delta H$, where $H=U+pV$ is enthalpy. Thus the corresponding warming balances use heat capacity at constant volume or heat capacity at constant pressure. Electrical or shaft work must be included separately when present. These endpoint balances do not require the actual exchange to be a reversible thermodynamic process.

A covered cup open to atmospheric pressure approximately realizes the second constraint when escaping material is negligible. A sealed rigid reaction vessel realizes the first; its surrounding water, vessel and immersed parts form the calibrated receiver. The reaction's outward heat equals the receiver's gain only after losses and ignition input have been accounted for. The distinction concerns the reaction boundary, even if its receiver is open to atmospheric pressure.^[ref]

A historical quantitative result appears in James Prescott Joule's On the Mechanical Equivalent of Heat (1850): Table IX gives $772.692$ foot-pounds of mechanical work per warming of one pound of water by one degree Fahrenheit, with weighing reduced to vacuum. His final rounded statement specifies water between $55$ and $60$ degrees Fahrenheit. He acknowledged residual vibration and sound as possible upward bias. This is an original reported conversion result, not the definition of the modern joule; the apparatus and resting controls are described in Joule's paddle-wheel experiment.^[ref]