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X
Economic Feasibility Analysis
Dr. Eng. Yulius Deddy Hermawan
Department of Chemical Engineering
UPN “Veteran” Yogyakarta
Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Outline
1. Fixed Capital
2. Working Capital
3. Manufacturing Cost
4. General Expenses
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Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
X.1.
FIXED CAPITAL
Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Fixed Capital
1. Purchased equipment
2. Installation
3. Piping
4. Instrumentation
5. Insulation
6. Electrical
7. Building
8. Land and yard improvements
9. Utilities…………+
Physical plant cost
(PPC)
10. Engineering and construction+
Direct plant cost
(DPC)
11. Contractor’s fee
12. Contingency+
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Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Elements of Direct Fixed Capital (DFC) Cost Estimate
A Total plant direct cost (TPDC) (physical cost)
1. Equipment purchased cost (PC) (bare cost) 1.00 X PC
2. Installation 43% PC; all fluid processing 47% PC 3. Process piping Solid: 10-20% PC
Solid-fluid: 14-43% PC Fluid: 43-86% PC 4. Instrumentation No auto control: 15% PC
Auto control: 30% PC Computer control: 40% PC 5. Insulation Low-temp. plants: 8% PC 6. Electrical Facilities 11% PC
7. Buildings 6-45% PC, fluid processing 15-70% PC, solid processing 8. Yard Improvement 16% PC
9. Auxiliary Facilities Existing: 0%: minor new: 15% Major additions: 15-40% PC
Completely new (grass roots) 40-140%
Σ = TPDC Method of Purchase Cost Factor
Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Method of Purchase Cost Factor B Total Plant Indirect Cost (TPIC)
10. Engineering 25% TPDC (normal) 11. Construction 30-35% TPDC: small jobs
40% TPDC: high labor jobs
Σ = TPIC
C Total Plant Cost (TPC) TPC = TPDC + TPIC D Direct Fixed Capital
12. Contractor’s fee 5-8% TPC
13. Contingency 5% TPC: established commercial project 10% TPC: process subject to change 20% TPC: speculative process
14. Size Factor contingency should be adjusted as follows X0.80: huge commercial plant
X1.00: standard plant
X1.3: experimental units, pilot plants, small additions
Σ = (12 + 13)
Department of Chemical Engineering - UPN “Veteran” Yogyakarta Page 4 of 16
Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Purchased Equipment Cost
Cost data are often presented as cost versus capacity charts, or
expressed as a power law of capacity
M
B B
E
C
Q
Q
C
Where
C
E= equipment cost with capacity
Q
C
B= known base cost for equipment with capacity
Q
BM
=
constant depending on equipment type
Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
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Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Purchased Equipment Cost
Such data can be brought up-to-date and
put on a common basis using cost indexes
2 1 2 1
INDEX
INDEX
C
C
Where
C
1= Equipment cost in year 1
C
2= Equipment cost in year 2
INDEX
1= Cost index in year 1
INDEX
2= Cost index in year 2
Delivery cost: up to 15% PEC
Cost Index references
:
•
Marshall & Stevens (MS)
•
Nelson refinery
•
Engineering News Record
•
Chem. Eng. Plant (CEP)
PEC + Delivery Cost = Delivered Equipment Cost
Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Installation Cost (%PEC)
Material Labor Total
Foundations 4 3 7
Platforms & support 7 4 11
Erection of equipment -- 25 25
11 32 43
Piping Cost (%PEC)
Material Labor Total
Solid 8 6 14
Solid – fluid 21 15 36
Fluid 49 37 86
Instrumentation Cost (%PEC)
Material Labor Total
Few or no controls 4 1 5
Some specific controls 12 3 15
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Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Insulation Cost (%PEC)
Material Labor Total
Insulation cost 3 5 8
Electrical Auxiliaries Cost (%PEC)
Building
(
depend on the location
)
Installed cost of substations, feeder, wiring: 10 – 15 % PEC
Cost in Indonesia (Rp………./m2)
Land & Yard Improvement
Cost in Indonesia
Utilitie
Estimated agree with designed utility unit (up to installed cost)
Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Engineering & Construction (%PEC)
Physical Plant Cost ($) E & C (%)
< 1.000.000 30
1.000.000 – 5.000.000 25
>5.000.000 20
Contractor’s fee
4 – 10% Direct Plant Cost (DPC)
Contingency
% DPC
Low 12
Average 15
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Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
X.2.
WORKING CAPITAL
Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Working Capital
1. Raw material inventory
estimate : 1 month supply at purchased value
2. In process inventory
estimate : 0.5 total manufacturing cost X total hold-up time
3. Product inventory
estimate :1 month production, value at manufacturing cost
4. Extended credit
estimate : 1 month production at sales value, or 2x manufacturing cost
5. Available cash
estimate : 1 month manufacturing cost
Note: monthly manufacturing cost
Estimate: Iw = rm(m+4M+0.5MQ)
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Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
X.3.
MANUFACTURING COST
Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Manufacturing Cost
1. Raw materials 2. Labor
3. Supervision 4. Maintenance 5. Plant supplies
6. Royalties and patents
7. Utilities +
Direct Manufacturing Cost 8. Payroll overhead
9. Laboratory 10. Plant overhead 11. Packaging
12. Shipping +
Indirect Manufacturing Cost 13. Depreciation
14. Property fixed
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Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Direct Manufacturing Cost
1. Raw Materials:
• Purchased cost + delivery expenses
• Amortized costs of catalyst
2. Labor:
Related to the production directly operator’s total salary average:
• 5 – 10% MC
• 15 – 20% MC for considerable handling
3. Supervision:
• Simple operations: 10% labor cost
• Complex operations: 25% labor cost
Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Direct Manufacturing Cost
5. Plant supplies:
Used in normal operation: gaskets, lubricants, charts;
Around 15% of maintenance cost
6. Royalties and patents:
1 – 5% sales price :
7. Utilities:
water, steam, power (electrical), fuel, etc. calculated based on the process
4. Maintenance:
Cost of materials and labor for routine maintenance and incidental repairs:
Annual maintenance
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Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Indirect Manufacturing Cost
8. Payroll overhead:
Pension, vacation, insurance, social security, 15 – 20% labor cost
9. Laboratory:
Quality control, 10 – 15% labor cost
10. Plant overhead:
health, trip (holiday), ware house, 50 – 100% labor cost
11. Packaging:
Food product 24% sales price Oil product 35% sales price
12. Shipping:
shipping cost
Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Fixed Manufacturing Cost
13. Depreciation:
as an economic plant
14. Property taxes:
1 – 2% Fixed Capital
15. Insurance:
Department of Chemical Engineering - UPN “Veteran” Yogyakarta Page 11 of 16
Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Typical labor requirements for process equipment
Type of equipment
Workers/Unit/Shift
Dryer, rotary
1/2
Dryer, spray
1
Dryer, tray
1/2
Centrifugal separator
1/2 – 1/4
Crystallizer, mechanical
1/6
Filter, vacuum
1/8 – 1/4
Evaporator
1/4
Reactor, batch
1
Reactor, continuous
1/2
Steam plant (100,000 lb/h)
3
Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Scale up of labor cost
Here
N
and
r
refer to the number of operators per shift and
plant capacity, respectively of two plants,
A
and
B
, different in
capacity, but producing the same product. The capacity
exponent is about 0.25
25
.
0
A
B
A
B
r
r
N
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Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
X.4.
GENERAL EXPENSES
Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
General Expenses
1. Administration
2 – 3%sales or 4 – 6% manufacturing cost
2. Sales: for promotion, 3 – 12% sales
3. Research: 2 – 4% sales
4. Finance:
pay interest (bank) for a loan (part of) Fixed Capital and Working Capital
the amount is = iF (FC.KF) + iw(WC.Kw)
Profit:
Sales ………
Manufacturing cost ………
General expense ………
Total cost ………
Profit before taxes ………
Taxes (up to 52%) ………
Profit after taxes ………
–
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Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Process Classification
(
in calculation of manufacturing cost
)
1. One main product:
production cost is loaded to a main product
2. Two or more of main products:
production cost is loaded to all main products based on:
•
production quantity,
•
product’s price
3. There is a sold byproduct:
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Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
X.5.
PROFITABILITY
Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Return on Investment (ROI)
Profit before/after tax
For Minimum ROI Standard, use profit before taxes
%
100
x
Capital
Fixed
Profit
ROI
Types
Low risk
High risk
Industrial chemical
11
44
Petroleum
16
39
Pulp and paper
18
40
Pharmaceutical
24
56
Paints
21
44
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Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Pay Out Time (POT)
on
Depreciati
Profit
Capital
Fixed
POT
Unit: year
Aries Newton:
Maximum limit:
Profit
Before
Tax
0
.
1
FC
Capital
Fixed
POT
Types
Low risk
High risk
Industrial chemical
5
2
Petroleum
5
2
Pulp and paper
4
2
Pharmaceutical
3
2
Paints
3
2
Fermentation products
3
2
Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
BEP and SDP Calculation
1. Fixed Cost:
Depreciation Taxes
Insurances
2. Variable cost:
Raw Materials Packaging Utilities Royalties
3. Regulated cost
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Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY
Break Even Point
Production Capacity (%)
0
100
Fixed Cost
Variable Cost
Regular cost
Sales
BEP
SDP
Rp/tahun
or
$/yr
SDP: Shut Down Point