Proposal for Ethylene Glycol Distillation Tower Presenters: Demetrius Henry Tyler Ware Craig Staton.
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Transcript of Proposal for Ethylene Glycol Distillation Tower Presenters: Demetrius Henry Tyler Ware Craig Staton.
Outline
Background
Process Flow
Design Details
Material and Energy Balances
Equipment Sizes and Design
Capital and Operating Costs
Overall Process Economics
Background
Reclaimed Ethylene Glycol from auto repair shops
25 mole% of Ethylene Glycol and Water
Provide a free service to get raw material
Use the r.m. to distill out nearly pure Ethylene Glycol to sell back
Design Details
Column height/diameter
Number of Plates
Plate height
Size of the re-boiler
Size of Condenser
Batch or Continuous
Piping
Material/Energy Balance (Condenser)
Condenser
Cond. Begin x y T (K) pA* pB*
0.541904 0.99 357.9458 1386.628 14.77288
Cond. End x y T (K) pA* pB*
0.99 0.999518 343.199 767.3067 5.183553
average x y T (K) Gamma A Gamma B
0.765952 0.999948 349.362 1.000179 1.072187P1= 1065.987 mmHgP2= 589.1259 mmHg
LambdaC 38870.75 Btu/kg-molQC= 699221.9 Btu/hr
Material/Energy Balance (Reboiler)
Reboiler
Reboiler End x y T (K) pA* pB*
0.006322 0.1 430.6352 11072.58 662.3231
Reboiler Begins x y T (K) pA* pB*
0.1 0.779687 401.019 5424.44 175.3823
average x y T (K) Gamma A Gamma B
0.053161 0.627563 411.3834 1.266893 1.027493P1= 535.9551 mmHgP2= 1390.082 mmHg
LambdaR 43728.29 Btu/kg-molQR= 786601.2 Btu/hr
Pumps
Product Storage Pump: Sized for 60 g/hr
Cost: $3,071.89
Feed Pump: Sized for 110 g/hr
Cost: $3,071.89
Pipe
Total Feet of Pipe: 480 ft.
Feed Diameter: 1.5 in.
Bottoms Diameter: 1.0 in.
Tops Diameter: 0.50 in.
Cooling Water Diameter: 2.5 in.
Cost: $1,754.37
Capital and Operating Costs
Total Capital (including installation, etc.)$301,442.59
Total Operating Cost (first year)$1,430,798.44
Cost per gallon$2.29
Price per gallon$3.50
Overall EconomicsProfit After 20 Years
-$500,000.00
$0.00
$500,000.00
$1,000,000.00
$1,500,000.00
$2,000,000.00
$2,500,000.00
0 2 4 6 8 10 12 14 16 18 20
Time (Years)
Pro
fit