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Department of Chemical Engineering - UPN “Veteran” Yogyakarta Page 1 of 16

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

(2)

Department of Chemical Engineering - UPN “Veteran” Yogyakarta Page 2 of 16

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+

(3)

Department of Chemical Engineering - UPN “Veteran” Yogyakarta Page 3 of 16

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)

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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

B

M

=

constant depending on equipment type

Dr. Eng. Y. D. Hermawan – ChemEng - UPNVY

(5)

Department of Chemical Engineering - UPN “Veteran” Yogyakarta Page 5 of 16

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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Department of Chemical Engineering - UPN “Veteran” Yogyakarta Page 6 of 16

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

(7)

Department of Chemical Engineering - UPN “Veteran” Yogyakarta Page 7 of 16

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)

(8)

Department of Chemical Engineering - UPN “Veteran” Yogyakarta Page 8 of 16

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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Department of Chemical Engineering - UPN “Veteran” Yogyakarta Page 9 of 16

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

(10)

Department of Chemical Engineering - UPN “Veteran” Yogyakarta Page 10 of 16

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:

(11)

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

(12)

Department of Chemical Engineering - UPN “Veteran” Yogyakarta Page 12 of 16

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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Department of Chemical Engineering - UPN “Veteran” Yogyakarta Page 13 of 16

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:

(14)

Department of Chemical Engineering - UPN “Veteran” Yogyakarta Page 14 of 16

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

(15)

Department of Chemical Engineering - UPN “Veteran” Yogyakarta Page 15 of 16

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

(16)

Department of Chemical Engineering - UPN “Veteran” Yogyakarta Page 16 of 16

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

Referensi

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