The Boltzmann temperature which corresponds to said matching emission spectrum is then associated to the chimioluminescent spectrum and the adiabatic flame temperature is derived from the Boltzmann temperature by correlation.

Consequently, the process temperature will increase by ΔTad reaching the Maximum Temperature of the Synthesis Reaction (MTSR).

See also Maximum temperature attainable by the synthesis reaction (MTSR).

Said temperature sensor measures the temporary adiabatic temperature increase during a side impact and a control device identifies a side impact based on said measured temperature increase and the temperature gradient.

By controlling the flows in this way, a calculated energy output or adiabatic flame temperature can be produced.

The mixtures of reaction precursor reagents are characterized by at least one reaction having an adiabatic temperature of at least 800 °C.

The method leverages the adiabatic temperature rise which occurs when the food is hydrostatically pressurized, coupled with the lethality of the pressure, to achieve appropriate sterilization conditions.

In another embodiment a liner is used having an adiabatic temperature rise of between 1 and 10 K per 100 MPa, preferably between 2 and 7 K per MPa.

The method includes increasing the adiabatic flame temperature of the low BTU natural gas using heavy hydrocarbons, wherein the heavy hydrocarbons include compounds with a carbon number of at least two.

The flames resulting from the combustion have an adiabatic flame temperature of above 1000°C, wherein, in the combustion of the fuel gas, at least some of the organic substances present in the fuel gas are cracked.