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Fresh feed and orts were sampled on the last 3 d of each treatment period for each heifer and were then subjected to particle size analysis.
Fresh feed and orts were sampled daily for each cow and subjected to neutral detergent fiber (NDF) and particle size analysis.
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.
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.
The fresh feed reacts at moderate operating conditions in the first stage riser to generate more diesel oil.
A cooling recycle stream, containing reaction products and a fresh feed, was included via a closed loop calculation.
An earlier study explored the design and control of the ammonia process given a fresh feed of hydrogen and nitrogen.
Treatments were ad libitum feeding with fresh feed delivery 1×/d at 0830 h or 2030 h.
The amount of fresh feed introduced per cycle and the injection width were identified as the only free operating parameters.
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