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We are designing a beverage plant to produce beverages sweetened with dextrose and no fructose or sucrose. Your task is to design a process to
We are designing a beverage plant to produce beverages sweetened with dextrose and no fructose or sucrose. Your task is to design a process to blend water and a concentrated dextrose syrup to produce two products. One product, containing dextrose, to be produced at the rate shown in Table below. This product will go to Area of the new plant. The other product, containing dextrose, to be produced at the rate shown in Table below. This product will go to Area of the new plant. The products should leave your area at gauge The concentration specifications for the products are average concentrations over a hour period. You will have two feeds available: Concentrated dextrose syrup at and bar gauge will be available at the concentration shown in Table below. Note that this concentration may vary over a range of Foodgrade water will be available at and bar gauge Please observe the following constrains: Mixing vessels should use pumparounds with a total flow rate of Size vessels to be about full under normal circumstances. Approximate mixing times at design conditions are as follows: To dilute concentrated dextrose to wt dextrose: min To dilute concentrated dextrose to dextrose: min To dilute wt dextrose to wt dextrose: min Your design should include controls for the feed and product stream flow rates, the product concentrations, and tank levels. You may neglect the dynamics of control valves and measuring devices.
We are designing a beverage plant to produce beverages sweetened with dextrose and no
fructose or sucrose. Your task is to design a process to blend water and a concentrated
dextrose syrup to produce two products.
One product, containing dextrose, to be produced at the rate shown
in Table below. This product will go to Area of the new plant.
The other product, containing dextrose, to be produced at the rate
shown in Table below. This product will go to Area of the new plant.
The products should leave your area at gauge The concentration specifications
for the products are average concentrations over a hour period.
You will have two feeds available:
Concentrated dextrose syrup at and bar gauge will be available at the
concentration shown in Table below. Note that this concentration may vary
over a range of
Foodgrade water will be available at and bar gauge
Please observe the following constrains:
Mixing vessels should use pumparounds with a total flow rate of
Size vessels to be about full under normal circumstances.
Approximate mixing times at design conditions are as follows:
To dilute concentrated dextrose to wt dextrose: min
To dilute concentrated dextrose to dextrose: min
To dilute wt dextrose to wt dextrose: min
Your design should include controls for the feed and product stream flow rates, the
product concentrations, and tank levels. You may neglect the dynamics of control valves
and measuring devices.
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