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The control structure thus obtained is unconventional with tight active constraint control requiring 'long' level loops that maintain the reflux drum and bottom sump levels of a column using the two process fresh feeds.
Results also show that the location of the fresh feeds is a dominant design variable with designs that do not constrain the feed tray location to be immediately above and below the reactive zone being substantially more economical.
I complained when Twitter was having ongoing problems; the withdrawal of not having fresh feeds is far far worse, although as an ex-Bloglines users I should be use to downtime of this nature by now.
The purpose of this paper is to study both the design and the control of a combined reformer/ammonia process in which steam-methane reforming, autothermal reforming and water-gas shift reactors are used to produce the hydrogen/nitrogen feed to the ammonia plant from fresh feeds of methane, water and air.
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The high temperature of the regeneration process (675 785 °C, or 1,250 1,450 °F) heats the catalyst to the desired reaction temperature for recontacting fresh feed into the unit.
Treatments were ad libitum feeding with fresh feed delivery 1×/d at 0830 h or 2030 h.
The aqueous phase is recycled by combining with the fresh feed.
The resulting fractions are then blended with fresh feed to match the given purity constraints.
Every day, 500 ml of digestate was removed from each reactor before adding another 500 ml of fresh feed.
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Since I tried Ludwig back in 2017, I have been constantly using it in both editing and translation. Ever since, I suggest it to my translators at ProSciEditing.

Justyna Jupowicz-Kozak
CEO of Professional Science Editing for Scientists @ prosciediting.com