Calorimeter sensor
AssigneeBayer Aktiengesellschaft
InventorsWilfried Litz, Adolf Schmidt, Ulrich Pallaske, Reinold Rose
Life of this patent
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Abstract
The invention relates to a process and an apparatus for determining the heat output rate in a reactor. This is achieved by determining the heat output rate in a sensor connected to the chemical reactor and taking into account the volume or mass ratio between the reactor and sensor contents. The apparatus allows balancing of the sensor, on the one hand, and continuous adjustment of the material composition and temperature of the reactor and sensor contents, on the other hand.
Claims7
A process for measuring the heat output rate in a reactor (3) with the aid of a calorimeter, which comprises a measuring cell (2), an intermediate thermostat (1) and a base thermostat (0), and taking as a basis the heat balance equation of the measuring cell (2)
- q.sub.Re +q.sub.Mi +q.sub.Ru2 +L.sub.2 +m.multidot.c.sub.3 .multidot.T.sub.3 -m.multidot.c.sub.2 .multidot.T.sub.2 =C.sub.2 .multidot.dT.sub.2 /dt+KF.sub.21 .multidot.(T.sub.2 -T.sub.1),
- with the quantity KF.sub.21 .multidot.(T.sub.2 -T.sub.1) being determined using the heat balance equation of the intermediate thermostat (1)
- KF.sub.21 .multidot.(T.sub.2 -T.sub.1)+L.sub.Ru1 +L.sub.1 =KF.sub.10 .multidot.(T.sub.1 -T.sub.0),
- in which
- C.sub.2 =effective heat capacity of the measuring cell content,
- q.sub.Re =heat output rate as a result of reaction in the measuring cell,
- q.sub.Mi =heat output rate as a result of mixing in the measuring cell,
- q.sub.Ru2 =heat output rate as a result of agitation in the measuring cell,
- L.sub.2 =electrical heat output in the measuring cell,
- m=mass flow through the measuring cell,
- C.sub.3 =specific heat of the inflow mass (production reactor),
- C.sub.2 =specific heat of the outflow mass (measuring cell),
- T.sub.3 =temperature of the production reactor,
- T.sub.2 =temperature of the measuring cell,
- T.sub.1 =temperature of the intermediate thermostat, and
- KF.sub.21 =diathermancy of the measuring cell to the intermediate thermostat;
- said process comprising the steps of:
- continuously adjusting the composition of the substance in the measuring cell (2) of the calorimeter to be the same as the composition of the substance in the reactor (3) (q.sub.mi =0 and c.sub.2 =c.sub.3);
- continuously adjusting the temperature of the substance in the measuring cell (2) to be the same as the temperature of the substance in the reactor (3) (m.multidot.c.sub.3 .multidot.T.sub.2 -m.multidot.c.sub.2 .multidot.T.sub.2 =0);
- interrupting the transport of substance from the reactor (3) into the measuring cell (2) for a period .delta.t;
- during said period .delta.t determining the effective heat capacity C.sub.2, taking as a basis the then prevailing heat balance equation
- C.sub.2 .multidot.dT.sub.2 /dt=q.sub.Re +q.sub.Ru2 -KF.sub.21 .multidot.(T.sub.2 -T.sub.1);
- determining the heat output rate q.sub.Re of the measuring cell (2) from the heat balance of the measuring cell (2);
- and
- determining the heat output rate in the reactor (3), taking into account at least one of the volume or mass ratio between the reactor and measuring cell contents.
In a calorimeter for measuring the heat output rate of a reactor, said calorimeter comprising a measuring cell (2), which has at least one temperature detector (6), a controllable heating device (5) with an output measuring circuit (7) and an agitator (4), an intermediate thermostat (1), which has at least one temperature detector (9) and a controllable heating device (11) with an output measuring circuit (17), and a base thermostat (0), with the controllable heating device (11) maintaining a constant temperature difference T.sub.1 between the base and the intermediate thermostat (0,1), the improvement wherein the calorimeter further comprises at least one connection (12) for transporting a substance from the reactor (3) into the measuring cell (2) of the calorimeter and a measurement and control unit (7) which adjusts the temperature in the measuring cell (2) to the temperature in the reactor (3).
Dependencies are inferred from the claim text.