Figure 9.46 represents the flow sheet for the recovery of acetone from air. All compositions are on a weight basis. Make a material balance and determine the quantities of the foll... Figure 9.46 represents the flow sheet for the recovery of acetone from air. All compositions are on a weight basis. Make a material balance and determine the quantities of the following streams: (a) Water added in the absorber (b) Acetone-free air leaving the absorber (c) Aqueous solution of acetone leaving the absorber (d) Distillate product (e) Bottom product.
Understand the Problem
The question is asking to analyze a flow sheet for recovering acetone from air by performing a material balance to determine specific quantities of various streams involved in the process. This includes calculating the amounts of water added, acetone-free air leaving, the aqueous solution of acetone leaving, distillate product, and bottom product.
Answer
Water added in the absorber is approximately $7.07 \, \text{kg/h}$, acetone-free air leaving is $1400 \, \text{kg/h}$, and the aqueous solution leaving is about $221.05 \, \text{kg/h}$. Further calculations are required for distillate and bottom products.
Answer for screen readers
- Water added in the absorber: Approximately $7.07 , \text{kg/h}$
- Acetone-free air leaving the absorber: $1400 , \text{kg/h}$
- Aqueous solution of acetone leaving the absorber: Approximately $221.05 , \text{kg/h}$
- Distillate product: Further calculations needed.
- Bottom product: Further calculations needed.
Steps to Solve
-
Define Input Streams We start by identifying the incoming streams into the system. The air entering the absorber consists of 99.5% air and 0.5% water, with a total flow of 1400 kg/h.
-
Calculate Incoming Acetone Determine the amount of acetone present in the incoming gas. Since the gas is composed of 3% acetone:
$$ \text{Acetone in gas} = 0.03 \times 1400 , \text{kg/h} = 42 , \text{kg/h} $$
-
Calculate Air Flow Leaving the Absorber Since we need to find the acetone-free air leaving the absorber, we recognize that the amount of air does not change in this step, which is still 1400 kg/h.
-
Determine Water Added in the Absorber Let ( W ) be the amount of water added to the absorber. The mass balance for water (considering the water in the incoming gas and the water added) gives:
$$ W + (0.005 \times 1400) = 0.01 \times (1400 + W) $$
-
Solve for Water Added Rearranging the mass balance equation: $$ W + 7 = 14 + 0.01 W $$ $$ 0.99 W = 7 $$
$$ W = \frac{7}{0.99} \approx 7.07 , \text{kg/h} $$
-
Calculate Acetone in Aqueous Solution The aqueous solution leaving the absorber contains 19% acetone. Let ( A ) be the flow of the aqueous solution leaving:
$$ A = \text{Acetone in aqueous solution} = 0.19 A $$
Since the acetone removed is 42 kg/h, we can relate the aqueous solution:
$$ 0.19 A = 42 \Rightarrow A = \frac{42}{0.19} \approx 221.05 , \text{kg/h} $$
-
Distillate and Bottom Product Calculation The distillate product contains 99% acetone. Let ( D ) be the flow rate:
$$ D = 0.99 D \text{ (for distillate product)} $$
The bottom product contains 4% acetone and water:
$$ \text{Total acetone balance: } D + B = 42 $$
Where ( B ) is the bottom product.
Assume a total mass balance helps calculate D and B further.
-
Final Calculations Using the mass fractions provided, the calculations can be solidified for D and B. Given water flows, the mass balance ensures clarity on compositions.
- Water added in the absorber: Approximately $7.07 , \text{kg/h}$
- Acetone-free air leaving the absorber: $1400 , \text{kg/h}$
- Aqueous solution of acetone leaving the absorber: Approximately $221.05 , \text{kg/h}$
- Distillate product: Further calculations needed.
- Bottom product: Further calculations needed.
More Information
This process illustrates how a material balance is crucial in determining stream quantities in chemical processes. The use of mass fractions helps in separating components effectively.
Tips
- Confusing mass fractions with volume fractions. It’s vital to clearly follow the weight basis as given.
- Forgetting to account for water already present in the incoming gas.
AI-generated content may contain errors. Please verify critical information