A new instrument, the Fugatron, is presented that was developed to make in situ measurements
of dissolved hydrogen concentrations in laboratory reactors. The principle of measurement is
based on a probe with a tip that consists of a small porous metal substrate coated with a dense
layer of fluoropolymer. The probe is exposed to the liquid phase and is internally purged by a
constant flow of carrier gas. Driven by the hydrogen concentration gradient between the external
and internal side of the composite layer, the hydrogen molecules permeate into the carrier gas
stream. The concentration of the permeate in the carrier gas stream is measured by a gas
analyzer. The analyzer signal is proportional to the partial pressure of dissolved gas. The steady-state concentration of dissolved hydrogen in the liquid is calculated from the analyzer signal by
using solubility data. Calibration methods are described for immersion probes used for in situ
measurements in reactors which are operated in batch or continuous mode as well as for flow-through probes used for liquid stream analysis. The sensitivity of the instrument and the
reliability of the measurements were tested in different solutions as a function of temperature
and pressure. The hydrogenation of an alkyne with a suspended palladium catalyst was chosen
as a model reaction for in situ measurements. The hydrogenation experiments were carried out
in a 0.5-L stirred-tank reactor with a turbine stirrer in a semibatch mode. Initial hydrogen
uptake rates and dissolved hydrogen concentrations during this model reaction were measured
as a function of the amount of catalyst in the liquid. The solubility of hydrogen in the pure
liquid was determined by a gas absorption measurement at reaction conditions. From these
measurements, the volumetric liquid-side mass transfer coefficient k
L
a at the gas−liquid interface
was calculated as a function of catalyst loading. In addition, the k
L
a value was also determined
in the absence of solid particles by the dynamic pressure drop method. Discrepancies that may
result from calculating steady-state dissolved hydrogen concentrations using k
L
a values obtained
from measurements conducted either in pure liquids or in liquids that contain suspended catalyst
particles are discussed and illustrated by these measurements. The new method allows direct
measurement of the concentrations of dissolved gases during a reaction, which can be a decisive
factor for the rate as well as for the selectivity of a process. Estimations of the gas concentrations
via reaction rate data and cumbersome determinations of k
L
a values are, therefore, no longer
necessary.