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After removing sulfur, the syngas stream is passed through the PSA-CO2 unit where CO2 is adsorbed by the adsorbent material (activated carbon) and the remaining gases (Tail gas 1; see Figure 1a) exits with a pressure drop of 0.49 atm.
The thin stillage, the condensed flash vapours and the liquid fraction of the pretreated slurry are fed to one UASB reactor with a volume of 790 m, with a retention time of 3 h and upflow velocity of 5 m/h, after which the stream is passed to five parallel second-stage UASB reactors, each with a volume of 1,740 m, with a retention time of 33 h and upflow velocity of 1 m/h.
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The other stream was passed through a copperised cadmium reductor column where reduction of nitrate to nitrite occurs, and the sample was then mixed with the reagent and passed through the cell of the spectrophotometer to be detected as nitrite plus nitrate.
Product solution was collected in the product collector and the hydrogen stream was passed through the gas liquid separator where the liquid phase was separated and pure hydrogen gas was released from the system.
The effluent gas stream was passed through a 1/4 inch ice trap and then directly into a flame ionization detector where the hydrocarbons released from the shale could be monitored over the course of reaction.
The air stream was passed over activated carbon and filtered through a 0.2 μm filter before being flushed into the reactors.
After demodulation, the bit streams are passed to the despreader which converts them to 4-bit symbols.
Figure 1 shows a filter bank based schematic baseband equivalent of transmultiplexer system, based on the LPTV theory parallel complex data streams are passed to subcarrier transmission filters.
Sensible wheel: Type 667c Uses a "constant effectiveness minimum capacitance" approach to model an air to air heat recovery device in which two air streams are passed near each other so that both energy and possibly moisture may be transferred between the streams.
From the interaction chamber, the streams were passed through a cooling loop to remove the heat produced during microfluidization and returned to the reservoir for recirculation and the process continued until a desired vesicles size was not produced [ 67].
A stream of H2 (99.9 % from Air Products) flow was passed through the catalyst at a GHSV of 5,000 8,000 h−1 under atmospheric pressure before reaction.
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