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The vehicle is also equipped by an auto-thermal reformer and, in order to minimize the hydrogen buffer size, the control algorithm is subject to constraints on the maximum hydrogen buffer level.
The refuelling system comprises a high concentrated PV array (CPV), an electrolyser, a hydrogen buffer tank and a diaphragm hydrogen compressor.
This means that the hydrogen buffer control has to negotiate how much energy can be stored, and act on the production system.
The system is composed of a water electrolysis unit, a hydrogen buffer tank, a metal hydride tank and a polymer electrolyte membrane fuel cell (PEMFC).
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This medium was buffered with 50 mM potassium hydrogen phthalate buffer (pH 5.2) and supplemented with hexose sugars to mimic the sugar composition in 100% hydrolysate.
Gel pieces were washed two times alternating with 50 m M ammonium hydrogen carbonate buffer and 25 m M ammonium hydrogen carbonate buffer with 50% acetonitrile.
The TMA was treated with 2.5% hydrogen peroxide/methanol buffer to inhibit endogenous peroxidase and boiled in a pressure cooker with sodium citrate buffer.
Therefore, diammonium hydrogen phosphate buffer was selected for analysis.
This paper shows the results of the grid-connected hydrogen energy buffer characterization, considering hydrogen production in this first stage.
YNB medium was supplemented with 20 g l-1 glucose, 50 mM potassium hydrogen phthalate buffer (Hahn-Hägerdal et al. 2005) and acetic acid.
Briefly, second stage suspension cultures were filtered and the cells were washed with di-potassium hydrogen phosphate buffer (pH 6.8) followed by distilled water.
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