financial analysis

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Technological Institute of the Philippines FINANCIAL ANALYSIS This is an outline of the economic considerations, which are necessary when preparing an estimate of the capital investment or total product cost for a new venture or project. Methods for obtaining predesign cost estimates has purposely been emphasized because the latter are extremely important for determining the feasibility of proposed investment and to compare alternative designs. The predesign estimates are based partially on approximate percentages or factor that are applicable to a particular plant or process under consideration. USE OF COST INDEXES A cost index is merely an index value for a given period point in time showing the cost at that time relative to a certain base time. If the cost at some time in the past is known, the equivalent cost at the present time can be determined by multiplying the original cost by the ratio of the present index value to the index value applicable when the original cost was obtained. For the Manufacture of Ammonium Nitrate by Prilling Process from Ammonia and Nitric acid, we used the Marshall and Swift Equipment Cost Indexes projected to 2013. We used the projections cost index Marshall and Swift Installed Equipment Indexes ( Reference: Chemical Engineering Plant Cost Index) YEAR X is the number of years since 2005 Y is the CEPCI 2005 0 468.2 2006 1 499.6 2007 2 525.4 2008 3 575.4 2009 4 521.9 2010 5 550.8 2011 6 585.7 2012 7 584.6 2013 8 567.6

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Page 1: Financial Analysis

Technological Institute of the Philippines

FINANCIAL ANALYSIS

This is an outline of the economic considerations, which are necessary when preparing an estimate of the capital investment or total product cost for a new venture or project.

Methods for obtaining predesign cost estimates has purposely been emphasized because the latter are extremely important for determining the feasibility of proposed investment and to compare alternative designs. The predesign estimates are based partially on

approximate percentages or factor that are applicable to a particular plant or process under consideration.

USE OF COST INDEXES

A cost index is merely an index value for a given period point in time showing the cost at

that time relative to a certain base time. If the cost at some time in the past is known, the equivalent cost at the present time can be determined by multiplying the original cost by the ratio of the present index value to the index value applicable when the original cost

was obtained.

For the Manufacture of Ammonium Nitrate by Prilling Process from Ammonia and Nitric acid, we used the Marshall and Swift Equipment Cost Indexes projected to 2013. We used the projections cost index

Marshall and Swift Installed Equipment Indexes (Reference: Chemical Engineering

Plant Cost Index)

YEAR X is the number of years since 2005

Y is the CEPCI

2005 0 468.2

2006 1 499.6

2007 2 525.4

2008 3 575.4

2009 4 521.9

2010 5 550.8

2011 6 585.7

2012 7 584.6

2013 8 567.6

Page 2: Financial Analysis

Technological Institute of the Philippines

By plotting the data above, we could get the cost index for the year 2015,

Using the Equation above

๐‘ฆ = โˆ’0.1211๐‘ฅ 6 + 2.051๐‘ฅ 5 โˆ’ 11.509๐‘ฅ 4 + 22.461๐‘ฅ 3 โˆ’ 6.5617๐‘ฅ 2 + 20.605๐‘ฅ+ 468.76

Where:

X=3

๐‘ฆ = โˆ’0.1211(3)6 + 2.051(3)5 โˆ’ 11.509(3)4 + 22.461(3)3 โˆ’ 6.5617(3)2

+ 20.605(3) + 468.76

๐’š = ๐Ÿ“๐Ÿ“๐Ÿ“.๐Ÿ–๐Ÿ“ (๐‘ช๐’๐’”๐’• ๐’Š๐’๐’…๐’†๐’™ ๐’‡๐’๐’“ ๐’š๐’†๐’‚๐’“ ๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“)

๐‘ช๐’๐’”๐’• ๐‘ฐ๐’๐’…๐’†๐’™ ๐’‚๐’• ๐Ÿ๐ŸŽ๐ŸŽ๐Ÿ = ๐Ÿ‘๐Ÿ—๐Ÿ“.๐Ÿ”

Exchange Rate (Source: www.bsp.gov.ph)

Unite States Dollar (USD) Philippine Peso (Php)

$1 Php 46.831

As of October 1, 2015

Page 3: Financial Analysis

Technological Institute of the Philippines

Cost Estimation

Estimation of Capital Investment

Plant Capacity:10000 kg/day

Plant Operation: 300 days/year at 8 hours/day

TOTAL COST OF PURCHASED EQUIPMENT

Equipment No. of

Equipment Total Cost Unit

Silo 1 374,648.00 PhP

Neutralizer 1 1,986,439.89 PhP

Vibrating Screen 1 448,547.32 PhP

Prill Tower 1 46,350,500.00 PhP

Dryer 1 2,056,872.78 PhP

Mixer 1 140,498.00 PhP

Flash Drum Evaporator 1 1,030,282.00 PhP

Evaporator 1 38,624,589.38 PhP

Shell and Tube Heat Exchanger (V-001) 1 573,283.56 PhP

Shell and Tube Heat Exchanger (HEX-001) 1 103,480.39 PhP

Shell and Tube Heat Exchanger (HEX-002) 1 628,634.99 PhP

Shell and Tube Heat Exchanger (HEX-006) 1 137,636.31 PhP

Double Pipe Heat Exchanger (HEX-003) 1 535,319.07 PhP

Double Pipe Heat Exchanger (HEX-004) 1 257,991.98 PhP

Double Pipe Heat Exchanger (HEX-005) 1 257,991.98 PhP

Rotary Cooler 1 468,310.00 PhP

Screw Conveyor 4 515,141.00 PhP

Total Purchase Equipment Cost w/ Delivery Cost 94,490,166.65 PhP

Page 4: Financial Analysis

Technological Institute of the Philippines

Cost of Equipment

* Using the McGraw Hill Online Cost Estimator

1. SILO

Heat transfer area: m2 Materials of Construction: Cost2002: PhP 374,648.00

Solving for Cost2015

Cost2015 = Cost 2002 (cost index at 2015

cost index at 2002)

Cost2015 = 374,648.00 (555.85

395.6)

๐‘ช๐’๐’”๐’•๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“ = ๐‘ท๐’‰๐‘ท ๐Ÿ“๐Ÿ๐Ÿ”,๐Ÿ’๐Ÿ๐ŸŽ.๐Ÿ•๐Ÿ“

2. NEUTRALIZER

Heat transfer area: m2 Materials of Construction: Carbon Steel Cost2002: PhP 1,986,439.89

Solving for Cost2015

Cost2015 = Cost 2002 (cost index at 2015

cost index at 2002)

Cost2015 = 1,986,439.89 (555.85

395.6)

๐‘ช๐’๐’”๐’•๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“ = ๐‘ท๐’‰๐‘ท ๐Ÿ,๐Ÿ•๐Ÿ—๐Ÿ,๐Ÿ๐ŸŽ๐Ÿ–.๐Ÿ•๐Ÿ‘ 3. VIBRATING SCREEN

Heat transfer area: m2 Materials of Construction: Cost2002: PhP 448,547.32

Solving for Cost2015

Cost2015 = Cost 2002 (cost index at 2015

cost index at 2002)

Cost2015 = 448,547.32 (555.85

395.6)

๐‘ช๐’๐’”๐’•๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“ = ๐‘ท๐’‰๐‘ท ๐Ÿ”๐Ÿ‘๐ŸŽ,๐Ÿ๐Ÿ’๐Ÿ“.๐Ÿ๐Ÿ•

4. PRILL TOWER Heat transfer area: m2

Materials of Construction: Cost2002: PhP 46,350,500.00 Solving for Cost2015

Cost2015 = Cost 2002 (cost index at 2015

cost index at 2002)

Cost2015 = 46,350,500.00 (555.85

395.6)

๐‘ช๐’๐’”๐’•๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“ = ๐‘ท๐’‰๐‘ท ๐Ÿ”๐Ÿ“,๐Ÿ๐Ÿ๐Ÿ”,๐Ÿ๐ŸŽ๐Ÿ.๐Ÿ•๐Ÿ–

Page 5: Financial Analysis

Technological Institute of the Philippines

5. DRYER Heat transfer area: m2 Materials of Construction:

Cost2002: PhP 2,056,872.78 Solving for Cost2015

Cost2015 = Cost 2002 (cost index at 2015

cost index at 2002)

Cost2015 = 2,056,872.78 (555.85

395.6)

๐‘ช๐’๐’”๐’•๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“ = ๐‘ท๐’‰๐‘ท ๐Ÿ,๐Ÿ–๐Ÿ—๐ŸŽ,๐ŸŽ๐Ÿ•๐Ÿ.๐Ÿ”๐Ÿ’ 6. MIXER

Heat transfer area: m2 Materials of Construction: Cost2002: PhP 140,498.00

Solving for Cost2015

Cost2015 = Cost 2002 (cost index at 2015

cost index at 2002)

Cost2015 = 140,498.00 (555.85

395.6)

๐‘ช๐’๐’”๐’•๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“ = ๐‘ท๐’‰๐‘ท ๐Ÿ๐Ÿ—๐Ÿ•,๐Ÿ’๐Ÿ๐Ÿ.๐ŸŽ๐Ÿ“ 7. FLASH DRUM EVAPORATOR

Heat transfer area: m2 Materials of Construction:

Cost2002: PhP 1,030,282.00 Solving for Cost2015

Cost2015 = Cost 2002 (cost index at 2015

cost index at 2002)

Cost2015 = 1,030,282.00 (555.85

395.6)

๐‘ช๐’๐’”๐’•๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“ = ๐‘ท๐’‰๐‘ท ๐Ÿ,๐Ÿ’๐Ÿ’๐Ÿ•,๐Ÿ”๐Ÿ๐Ÿ—.๐Ÿ“๐Ÿ“ 8. EVAPORATOR

Heat transfer area: 40.93 m2 Materials of Construction: Carbon Steel & Stainless Steel Cost2002: PhP 38,624,589.38

Solving for Cost2015

Cost2015 = Cost 2002 (cost index at 2015

cost index at 2002)

Cost2015 = 38,624,589.38 (555.85

395.6)

๐‘ช๐’๐’”๐’•๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“ = ๐‘ท๐’‰๐‘ท ๐Ÿ“๐Ÿ’๐Ÿ๐Ÿ•๐ŸŽ๐Ÿ”๐Ÿ•๐Ÿ.๐Ÿ’๐Ÿ

Page 6: Financial Analysis

Technological Institute of the Philippines

9. SHELL AND TUBE HEAT EXCHANGER (V-001) Heat transfer area: m2 Materials of Construction:

Cost2002: PhP 573,283.56 Solving for Cost2015

Cost2015 = Cost 2002 (cost index at 2015

cost index at 2002)

Cost2015 = 573,283.56 (555.85

395.6)

๐‘ช๐’๐’”๐’•๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“ = ๐‘ท๐’‰๐‘ท ๐Ÿ–๐ŸŽ๐Ÿ“,๐Ÿ“๐ŸŽ๐Ÿ—.๐Ÿ•๐Ÿ• 10. SHELL AND TUBE HEAT EXCHANGER (HEX-001)

Heat transfer area: m2 Materials of Construction: Cost2002: PhP 103,480.39

Solving for Cost2015

Cost2015 = Cost 2002 (cost index at 2015

cost index at 2002)

Cost2015 = 103,480.39 (555.85

395.6)

๐‘ช๐’๐’”๐’•๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“ = ๐‘ท๐’‰๐‘ท ๐Ÿ๐Ÿ’๐Ÿ“,๐Ÿ‘๐Ÿ—๐Ÿ–.๐Ÿ‘๐Ÿ

11. SHELL AND TUBE HEAT EXCHANGER (HEX-002) Heat transfer area: 3.8704 m2 Materials of Construction: 304 Stainless Steel

Cost2002: PhP 628,634.99 Solving for Cost2015

Cost2015 = Cost 2002 (cost index at 2015

cost index at 2002)

Cost2015 = 628,634.99 (555.85

395.6)

๐‘ช๐’๐’”๐’•๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“ = ๐‘ท๐’‰๐‘ท ๐Ÿ–๐Ÿ–๐Ÿ‘,๐Ÿ๐Ÿ–๐Ÿ‘.๐ŸŽ๐Ÿ 12. SHELL AND TUBE HEAT EXCHANGER (HEX-006)

Heat transfer area: m2 Materials of Construction: Cost2002: PhP 137,636.31

Solving for Cost2015

Cost2015 = Cost 2002 (cost index at 2015

cost index at 2002)

Cost2015 = 137,636.31 (555.85

395.6)

๐‘ช๐’๐’”๐’•๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“ = ๐‘ท๐’‰๐‘ท ๐Ÿ๐Ÿ—๐Ÿ‘,๐Ÿ‘๐Ÿ—๐ŸŽ.๐Ÿ๐Ÿ“

Page 7: Financial Analysis

Technological Institute of the Philippines

13. DOUBLE PIPE HEAT EXCHANGER (HEX-003) Heat transfer area: m2 Materials of Construction:

Cost2002: PhP 535,319.07 Solving for Cost2015

Cost2015 = Cost 2002 (cost index at 2015

cost index at 2002)

Cost2015 = 535,319.07 (555.85

395.6)

๐‘ช๐’๐’”๐’•๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“ = ๐‘ท๐’‰๐‘ท ๐Ÿ•๐Ÿ“๐Ÿ,๐Ÿ๐Ÿ”๐Ÿ”.๐Ÿ”๐ŸŽ 14. DOUBLE PIPE HEAT EXCHANGER (HEX-004)

Heat transfer area: m2 Materials of Construction: Cost2002: PhP 257,991.98

Solving for Cost2015

Cost2015 = Cost 2002 (cost index at 2015

cost index at 2002)

Cost2015 = 257,991.98 (555.85

395.6)

๐‘ช๐’๐’”๐’•๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“ = ๐‘ท๐’‰๐‘ท ๐Ÿ‘๐Ÿ”๐Ÿ,๐Ÿ’๐Ÿ—๐Ÿ—.๐Ÿ”๐ŸŽ 15. DOUBLE PIPE HEAT EXCHANGER (HEX-005)

Heat transfer area: m2 Materials of Construction:

Cost2002: PhP 257,991.98 Solving for Cost2015

Cost2015 = Cost 2002 (cost index at 2015

cost index at 2002)

Cost2015 = 257,991.98 (555.85

395.6)

๐‘ช๐’๐’”๐’•๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“ = ๐‘ท๐’‰๐‘ท ๐Ÿ‘๐Ÿ”๐Ÿ,๐Ÿ’๐Ÿ—๐Ÿ—.๐Ÿ”๐ŸŽ 16. ROTARY COOLER

Heat transfer area: 2.66 m2 Materials of Construction: Cost2002: PhP 468,319.00

Solving for Cost2015

Cost2015 = Cost 2002 (cost index at 2015

cost index at 2002)

Cost2015 = 468,319.00 (555.85

395.6)

๐‘ช๐’๐’”๐’•๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“ = ๐‘ท๐’‰๐‘ท ๐Ÿ”๐Ÿ“๐Ÿ–,๐ŸŽ๐Ÿ๐Ÿ”.๐ŸŽ๐Ÿ–

Page 8: Financial Analysis

Technological Institute of the Philippines

17. SCREW CONVEYOR (4 UNITS) Heat transfer area: m2 Materials of Construction:

Cost2002: PhP 515,141.00 Solving for Cost2015

Cost2015 = Cost 2002 (cost index at 2015

cost index at 2002)

Cost2015 = 515,141.00 (555.85

395.6)

๐‘ช๐’๐’”๐’•๐Ÿ๐ŸŽ๐Ÿ๐Ÿ“ = ๐‘ท๐’‰๐‘ท ๐Ÿ•๐Ÿ๐Ÿ‘,๐Ÿ–๐Ÿ๐Ÿ‘.๐Ÿ‘๐Ÿ•

It is assumed that delivery charges are 5% of the purchased price.

๐‘‡๐‘œ๐‘ก๐‘Ž๐‘™ ๐‘ƒ๐‘ข๐‘Ÿ๐‘โ„Ž๐‘Ž๐‘ ๐‘’๐‘‘ ๐ถ๐‘œ๐‘ ๐‘ก = ๐‘ƒโ„Ž๐‘ 132,766,338.7

๐‘‡๐‘œ๐‘ก๐‘Ž๐‘™ ๐‘ƒ๐‘ข๐‘Ÿ๐‘โ„Ž๐‘Ž๐‘ ๐‘’๐‘‘ ๐ถ๐‘œ๐‘ ๐‘ก ๐‘ค๐‘–๐‘กโ„Ž ๐‘‘๐‘’๐‘™๐‘–๐‘ฃ๐‘’๐‘Ÿ๐‘ฆ ๐ถ๐‘œ๐‘ ๐‘ก

= ๐‘ƒโ„Ž๐‘ 132,766,338.7 + (0.05 ๐‘ฅ ๐‘ƒโ„Ž๐‘ 132,766,338.7)

๐‘ป๐’๐’•๐’‚๐’ ๐‘ท๐’–๐’“๐’„๐’‰๐’‚๐’”๐’†๐’… ๐‘ช๐’๐’”๐’• ๐’˜๐’Š๐’•๐’‰ ๐‘ซ๐’†๐’๐’Š๐’—๐’†๐’“๐’š ๐‘ช๐’๐’”๐’• (๐‘ท๐‘น๐‘ถ๐‘ช๐‘ฌ๐‘บ๐‘บ๐‘ฐ๐‘ต๐‘ฎ ๐‘ฌ๐‘ธ๐‘ผ๐‘ฐ๐‘ท๐‘ด๐‘ฌ๐‘ต๐‘ป)

= ๐‘ท๐’‰๐‘ท ๐Ÿ๐Ÿ‘๐Ÿ—,๐Ÿ’๐ŸŽ๐Ÿ’,๐Ÿ”๐Ÿ“๐Ÿ“.๐Ÿ”๐ŸŽ

Page 9: Financial Analysis

Technological Institute of the Philippines

Instrumentation and Control Cost

The scope of the instrumentation and control cost comprises the purchase and installation labor cost of auxillary machines, such as pressure and temperature gauges or flow controller, used to control equipment.

Total Instrumentation Cost (Alibaba.com)

Name of Instrumentation No. of Units

Price per unit, Php

Total Price, Php

Ball Valve 10

Check Valve 3

Conveyor Speeder 15

Flow Controller 3

Flow Transmitter 3

Level Transmitter 10

Orifice 3

Pump 3

Speed Controller 15

Summation controller 3

Temperature transmitter 2

Transducer 16

Weight Controller 10

Weight Transmitter 14

Total 6,024,000.00

Page 10: Financial Analysis

Technological Institute of the Philippines

I.DIRECT COSTS

Installation Cost

The scope of the installation cost of the equipment comprises the cost of foundation

support platforms, labor cost, construction related expense, and other factors related to the erection of the purchased equipment.

Basis: for a solid processing plant, 45% of the delivered equipment cost is the amount of the purchased equipment installed.

๐‘ƒ๐‘ข๐‘Ÿ๐‘โ„Ž๐‘Ž๐‘ ๐‘’๐‘‘ ๐ธ๐‘ž๐‘ข๐‘–๐‘๐‘š๐‘’๐‘›๐‘ก ๐ผ๐‘›๐‘ ๐‘ก๐‘Ž๐‘™๐‘™๐‘Ž๐‘ก๐‘–๐‘œ๐‘›= 0.45 ๐‘ฅ (๐‘‡๐‘œ๐‘ก๐‘Ž๐‘™ ๐‘‘๐‘™๐‘–๐‘ฃ๐‘’๐‘Ÿ๐‘’๐‘‘ โˆ’ ๐‘’๐‘ž๐‘ข๐‘–๐‘๐‘š๐‘’๐‘›๐‘ก ๐‘๐‘œ๐‘ ๐‘ก)

๐‘ƒ๐‘ข๐‘Ÿ๐‘โ„Ž๐‘Ž๐‘ ๐‘’๐‘‘ ๐ธ๐‘ž๐‘ข๐‘–๐‘๐‘š๐‘’๐‘›๐‘ก ๐ผ๐‘›๐‘ ๐‘ก๐‘Ž๐‘™๐‘™๐‘Ž๐‘ก๐‘–๐‘œ๐‘› = 0.45 ๐‘ฅ ๐‘ƒโ„Ž๐‘ 139,404,655.60

๐‘ท๐’–๐’“๐’„๐’‰๐’‚๐’”๐’†๐’… ๐‘ฌ๐’’๐’–๐’Š๐’‘๐’Ž๐’†๐’๐’• ๐‘ฐ๐’๐’”๐’•๐’‚๐’๐’๐’‚๐’•๐’Š๐’๐’ = ๐‘ท๐’‰๐’‘ ๐Ÿ”๐Ÿ,๐Ÿ•๐Ÿ‘๐Ÿ,๐ŸŽ๐Ÿ—๐Ÿ“.๐ŸŽ๐Ÿ

Piping and Conveyor Installation

The scope of the piping and conveyor installation comprises the labor cost of installation, cost of pipes, valves, fittings and all other piping and conveyor requirements.

Basis: 31% of the cost of purchased equipment delivered is the piping and conveyor cost installation.

๐‘ƒ๐‘–๐‘๐‘–๐‘›๐‘” ๐‘Ž๐‘›๐‘‘ ๐‘๐‘œ๐‘›๐‘ฃ๐‘’๐‘ฆ๐‘œ๐‘Ÿ ๐‘–๐‘›๐‘ ๐‘ก๐‘Ž๐‘™๐‘™๐‘Ž๐‘ก๐‘–๐‘œ๐‘›= 0.16 ๐‘ฅ (๐‘‡๐‘œ๐‘ก๐‘Ž๐‘™ ๐‘‘๐‘’๐‘™๐‘–๐‘ฃ๐‘’๐‘Ÿ๐‘’๐‘‘ โˆ’ ๐‘’๐‘ž๐‘ข๐‘–๐‘๐‘š๐‘’๐‘›๐‘ก ๐‘๐‘œ๐‘ ๐‘ก)

๐‘ƒ๐‘–๐‘๐‘–๐‘›๐‘” ๐‘Ž๐‘›๐‘‘ ๐‘๐‘œ๐‘›๐‘ฃ๐‘’๐‘ฆ๐‘œ๐‘Ÿ ๐‘–๐‘›๐‘ ๐‘ก๐‘Ž๐‘™๐‘™๐‘Ž๐‘ก๐‘–๐‘œ๐‘› = 0.31 ๐‘ฅ ๐‘ƒโ„Ž๐‘ 139,404,655.60

๐‘ท๐’Š๐’‘๐’Š๐’๐’ˆ ๐’‚๐’๐’… ๐’„๐’๐’๐’—๐’†๐’š๐’๐’“ ๐’Š๐’๐’”๐’•๐’‚๐’๐’๐’‚๐’•๐’Š๐’๐’ = ๐‘ท๐’‰๐’‘ ๐Ÿ’๐Ÿ‘,๐Ÿ๐Ÿ๐Ÿ“,๐Ÿ’๐Ÿ’๐Ÿ‘.๐Ÿ๐Ÿ’

Electrical Systems

The scope of the electrical system cost comprises the power, wiring, lightning,

transformation, service and instrumentation and control wiring.

Basis: 10% of the delivered equipment cost is the installed electrical system cost.

๐‘’๐‘™๐‘’๐‘๐‘ก๐‘Ÿ๐‘–๐‘๐‘Ž๐‘™ ๐‘ ๐‘ฆ๐‘ ๐‘ก๐‘’๐‘š ๐‘–๐‘›๐‘ ๐‘ก๐‘Ž๐‘™๐‘™๐‘Ž๐‘ก๐‘–๐‘œ๐‘›

= 0.10 ๐‘ฅ (๐‘‡๐‘œ๐‘ก๐‘Ž๐‘™ ๐‘‘๐‘’๐‘™๐‘–๐‘ฃ๐‘’๐‘Ÿ๐‘’๐‘‘ โˆ’ ๐‘’๐‘ž๐‘ข๐‘–๐‘๐‘š๐‘’๐‘›๐‘ก ๐‘๐‘œ๐‘ ๐‘ก)

๐‘’๐‘™๐‘’๐‘๐‘ก๐‘Ÿ๐‘–๐‘๐‘Ž๐‘™ ๐‘ ๐‘ฆ๐‘ ๐‘ก๐‘’๐‘š ๐‘–๐‘›๐‘ ๐‘ก๐‘Ž๐‘™๐‘™๐‘Ž๐‘ก๐‘–๐‘œ๐‘› = 0.10 ๐‘ฅ ๐‘ƒโ„Ž๐‘ 139,404,655.60

๐’†๐’๐’†๐’„๐’•๐’“๐’Š๐’„๐’‚๐’ ๐’”๐’š๐’”๐’•๐’†๐’Ž ๐’Š๐’๐’”๐’•๐’‚๐’๐’๐’‚๐’•๐’Š๐’๐’ = ๐‘ท๐’‰๐‘ท ๐Ÿ๐Ÿ‘,๐Ÿ—๐Ÿ’๐ŸŽ,๐Ÿ’๐Ÿ”๐Ÿ“.๐Ÿ“๐Ÿ”

Page 11: Financial Analysis

Technological Institute of the Philippines

Yard Improvement

The scope of the yard improvement comprises the roads, grading,fencing, sidewalks, railroads, sidings, landscaping, and any other similar items related to yard improvements.

Basis: for a solid processing plant, 15% of the delivered equipment cost is the yard improvement cost.

๐‘ฆ๐‘Ž๐‘Ÿ๐‘‘ ๐‘–๐‘š๐‘๐‘Ÿ๐‘œ๐‘ฃ๐‘’๐‘›๐‘ก = 0.15 ๐‘ฅ (๐‘‡๐‘œ๐‘ก๐‘Ž๐‘™ ๐‘‘๐‘’๐‘™๐‘–๐‘ฃ๐‘’๐‘Ÿ๐‘’๐‘‘ โˆ’ ๐‘’๐‘ž๐‘ข๐‘–๐‘๐‘š๐‘’๐‘›๐‘ก ๐‘๐‘œ๐‘ ๐‘ก)

๐‘ฆ๐‘Ž๐‘Ÿ๐‘‘ ๐‘–๐‘š๐‘๐‘Ÿ๐‘œ๐‘ฃ๐‘’๐‘›๐‘ก = 0.15 ๐‘ฅ ๐‘ƒโ„Ž๐‘ 139,404,655.60

๐’š๐’‚๐’“๐’… ๐’Š๐’Ž๐’‘๐’“๐’๐’—๐’†๐’๐’• = ๐‘ท๐’‰๐‘ท ๐Ÿ๐ŸŽ,๐Ÿ—๐Ÿ๐ŸŽ,๐Ÿ”๐Ÿ—๐Ÿ–.๐Ÿ‘๐Ÿ’

Service Facilities

The scope of service facilities comprises the utilities for supplying steam, water, power, and fuel for the chemical processes and operations. Fire protection, waste disposal and

miscellaneous service items such as shops, clinics or first aid quarters, and cafeterias require capital investment that are included under general heading of service facilities.

Basis: For a solid processing plant, the 40% of the delivered equipment cost is the service facility cost.

๐‘ ๐‘’๐‘Ÿ๐‘ฃ๐‘–๐‘๐‘’ ๐‘“๐‘Ž๐‘๐‘–๐‘™๐‘–๐‘ก๐‘ฆ ๐‘–๐‘›๐‘ ๐‘ก๐‘Ž๐‘™๐‘™๐‘Ž๐‘ก๐‘–๐‘œ๐‘›= 0.40 ๐‘ฅ (๐‘‡๐‘œ๐‘ก๐‘Ž๐‘™ ๐‘‘๐‘’๐‘™๐‘–๐‘ฃ๐‘’๐‘Ÿ๐‘’๐‘‘ โˆ’ ๐‘’๐‘ž๐‘ข๐‘–๐‘๐‘š๐‘’๐‘›๐‘ก ๐‘๐‘œ๐‘ ๐‘ก)

๐‘ ๐‘’๐‘Ÿ๐‘ฃ๐‘–๐‘๐‘’ ๐‘“๐‘Ž๐‘๐‘–๐‘™๐‘–๐‘ก๐‘ฆ ๐‘–๐‘›๐‘ ๐‘ก๐‘Ž๐‘™๐‘™๐‘Ž๐‘ก๐‘–๐‘œ๐‘› = 0.40 ๐‘ฅ ๐‘ƒโ„Ž๐‘ 139,404,655.60

๐’”๐’†๐’“๐’—๐’Š๐’„๐’† ๐’‡๐’‚๐’„๐’Š๐’๐’Š๐’•๐’š ๐’Š๐’๐’”๐’•๐’‚๐’๐’๐’‚๐’•๐’Š๐’๐’ = ๐‘ท๐’‰๐’‘ ๐Ÿ“๐Ÿ“๐Ÿ•๐Ÿ”๐Ÿ๐Ÿ–๐Ÿ”๐Ÿ.๐Ÿ๐Ÿ’

Total Direct Plant Cost:

๐‘ท๐’‰๐’‘ = ๐Ÿ๐Ÿ•๐Ÿ’๐Ÿ’๐Ÿ“๐Ÿ๐Ÿ“๐ŸŽ๐Ÿ’.๐Ÿ–

INDIRECT COSTS

Engineering and Supervision

Page 12: Financial Analysis

Technological Institute of the Philippines

The scope of the engineering and supervision comprises the internal or licensed software, computer-aided drafts, purchasing, accounting, travel, and the plant

supervisory services.

Basis: for a solid processing plant, 33% of the delivered equipment cost is the

engineering and supervision cost.

๐‘’๐‘›๐‘”๐‘–๐‘›๐‘’๐‘’๐‘Ÿ๐‘–๐‘›๐‘” ๐‘Ž๐‘›๐‘‘ ๐‘ ๐‘ข๐‘๐‘’๐‘Ÿ๐‘ฃ๐‘–๐‘ ๐‘–๐‘œ๐‘›

= 0.33 ๐‘ฅ (๐‘‡๐‘œ๐‘ก๐‘Ž๐‘™ ๐‘‘๐‘’๐‘™๐‘–๐‘ฃ๐‘’๐‘Ÿ๐‘’๐‘‘ โˆ’ ๐‘’๐‘ž๐‘ข๐‘–๐‘๐‘š๐‘’๐‘›๐‘ก ๐‘๐‘œ๐‘ ๐‘ก)

๐‘’๐‘›๐‘”๐‘–๐‘›๐‘’๐‘’๐‘Ÿ๐‘–๐‘›๐‘” ๐‘Ž๐‘›๐‘‘ ๐‘ ๐‘ข๐‘๐‘’๐‘Ÿ๐‘ฃ๐‘–๐‘ ๐‘–๐‘œ๐‘› = 0.33 ๐‘ฅ ๐‘ƒโ„Ž๐‘ 119,452,840.3

๐’†๐’๐’ˆ๐’Š๐’๐’†๐’†๐’“๐’Š๐’๐’ˆ ๐’‚๐’๐’… ๐’”๐’–๐’‘๐’†๐’“๐’—๐’Š๐’”๐’Š๐’๐’ = ๐‘ท๐’‰๐’‘ ๐Ÿ‘๐Ÿ—๐Ÿ’๐Ÿ๐Ÿ—๐Ÿ’๐Ÿ‘๐Ÿ•.๐Ÿ–๐Ÿ

Construction Expenses The scope of the construction expenses comprises the cost construction labor and other construction related expenses such as the construction tools and rentals,

construction payroll, construction tariffs, insurance and permits, miscellaneous equipment installation and other fees related to the construction process. Basis: for solid processing plant, 39% of the delivered equipment cost is the

construction expenses

๐‘๐‘œ๐‘›๐‘ ๐‘ก๐‘Ÿ๐‘ข๐‘๐‘ก๐‘–๐‘œ๐‘› ๐‘’๐‘ฅ๐‘๐‘’๐‘›๐‘ ๐‘’๐‘  = 0.39 ๐‘ฅ (๐‘‡๐‘œ๐‘ก๐‘Ž๐‘™ ๐‘‘๐‘’๐‘™๐‘–๐‘ฃ๐‘’๐‘Ÿ๐‘’๐‘‘ โˆ’ ๐‘’๐‘ž๐‘ข๐‘–๐‘๐‘š๐‘’๐‘›๐‘ก ๐‘๐‘œ๐‘ ๐‘ก)

๐‘๐‘œ๐‘›๐‘ ๐‘ก๐‘Ÿ๐‘ข๐‘๐‘ก๐‘–๐‘œ๐‘› ๐‘’๐‘ฅ๐‘๐‘’๐‘›๐‘ ๐‘’๐‘  = 0.39 ๐‘ฅ ๐‘ƒโ„Ž๐‘ 119,452,840.3

๐’„๐’๐’๐’”๐’•๐’“๐’–๐’„๐’•๐’Š๐’๐’ ๐’†๐’™๐’‘๐’†๐’๐’”๐’†๐’” = ๐‘ท๐’‰๐’‘ ๐Ÿ’๐Ÿ”๐Ÿ“๐Ÿ–๐Ÿ”๐Ÿ”๐ŸŽ๐Ÿ•.๐Ÿ•๐Ÿ‘

Legal Expenses

The scope of legal expenses comprises the costs related to the processing of land purchase, equipment purchase, and contracts of construction. Understanding and

proving compliance to government requirements, such as environmental and safety measures requirements constitute major sources of legal cost.

Basis: for solid processing equipment, 4% of the delivered equipment cost is the legal expenses.

๐‘™๐‘’๐‘”๐‘Ž๐‘™ ๐‘’๐‘ฅ๐‘๐‘’๐‘›๐‘ ๐‘’๐‘  = 0.04 ๐‘ฅ (๐‘‡๐‘œ๐‘ก๐‘Ž๐‘™ ๐‘‘๐‘’๐‘™๐‘–๐‘ฃ๐‘’๐‘Ÿ๐‘’๐‘‘ โˆ’ ๐‘’๐‘ž๐‘ข๐‘–๐‘๐‘š๐‘’๐‘›๐‘ก ๐‘๐‘œ๐‘ ๐‘ก)

๐‘™๐‘’๐‘”๐‘Ž๐‘™ ๐‘’๐‘ฅ๐‘๐‘’๐‘›๐‘ ๐‘’๐‘  = 0.04 ๐‘ฅ ๐‘ƒโ„Ž๐‘ 119,452,840.3

๐’๐’†๐’ˆ๐’‚๐’ ๐’†๐’™๐’‘๐’†๐’๐’”๐’†๐’” = ๐‘ท๐’‰๐’‘ ๐Ÿ’๐Ÿ•๐Ÿ•๐Ÿ–๐Ÿ๐Ÿ๐Ÿ‘.๐Ÿ”๐Ÿ๐Ÿ‘

Contractorโ€™s Fee

Page 13: Financial Analysis

Technological Institute of the Philippines

The scope of the contractorโ€™s fee includes the payment given to the construction company hired for the construction of the plant.

Basis: for solid processing equipment, 17% of the delivered equipment cost is the contractorโ€™s fee.

๐‘๐‘œ๐‘›๐‘ก๐‘Ÿ๐‘Ž๐‘๐‘ก๐‘œ๐‘Ÿโ€ฒ๐‘ ๐‘“๐‘’๐‘’ = 0.17 ๐‘ฅ (๐‘‡๐‘œ๐‘ก๐‘Ž๐‘™ ๐‘‘๐‘’๐‘™๐‘–๐‘ฃ๐‘’๐‘Ÿ๐‘’๐‘‘ โˆ’ ๐‘’๐‘ž๐‘ข๐‘–๐‘๐‘š๐‘’๐‘›๐‘ก ๐‘๐‘œ๐‘ ๐‘ก)

๐‘๐‘œ๐‘›๐‘ก๐‘Ÿ๐‘Ž๐‘๐‘ก๐‘œ๐‘Ÿโ€ฒ๐‘ ๐‘“๐‘’๐‘’ = 0.17 ๐‘ฅ ๐‘ƒโ„Ž๐‘ 119,452,840.3

๐’„๐’๐’๐’•๐’“๐’‚๐’„๐’•๐’๐’“โ€ฒ๐’”๐’‡๐’†๐’† = ๐‘ท๐’‰๐’‘ ๐Ÿ๐ŸŽ๐Ÿ‘๐ŸŽ๐Ÿ”๐Ÿ—๐Ÿ–๐Ÿ.๐Ÿ–๐Ÿ“ Contingency

The scope of the contingency comprises the estimation of the project cost in recognition of the fact that unexpected events and expenses that inevitably increase the cost of the project might arise during the erection of the plant. Inevitable events

such as storm, flood, transportation accidents, strikes, price changes, errors of the estimation, and unforeseen expenses may occur.

Basis: 37% of the purchase equipment delivered is the contingency.

๐‘๐‘œ๐‘›๐‘ก๐‘–๐‘›๐‘”๐‘’๐‘›๐‘๐‘ฆ = 0.37(๐‘๐‘ข๐‘Ÿ๐‘โ„Ž๐‘Ž๐‘ ๐‘’ ๐‘’๐‘ž๐‘ข๐‘–๐‘๐‘š๐‘’๐‘›๐‘ก ๐‘‘๐‘’๐‘™๐‘–๐‘ฃ๐‘’๐‘Ÿ๐‘’๐‘‘)

๐‘๐‘œ๐‘›๐‘ก๐‘–๐‘›๐‘”๐‘’๐‘›๐‘๐‘ฆ = 0.37 ๐‘ฅ ๐‘ƒโ„Ž๐‘ 119,452,840.3

๐’„๐’๐’๐’•๐’Š๐’๐’ˆ๐’†๐’๐’„๐’š = ๐‘ท๐’‰๐’‘ ๐Ÿ’๐Ÿ’๐Ÿ๐Ÿ—๐Ÿ•๐Ÿ“๐Ÿ“๐ŸŽ.๐Ÿ—๐Ÿ

Total Indirect Plant Cost:

๐‘ท๐’‰๐’‘ = ๐Ÿ๐Ÿ“๐Ÿ“๐Ÿ๐Ÿ–๐Ÿ–๐Ÿ•๐Ÿ–๐Ÿ’

RAW MATERIALS

Anyhdrous Liquid Ammonia

๐ถ = (2528.45 ๐‘˜๐‘”

๐‘‘๐‘Ž๐‘ฆ๐‘ฅ

1 ๐‘‘๐‘Ž๐‘ฆ

24 โ„Ž๐‘Ÿ๐‘ ) ๐‘ฅ 2400 โ„Ž๐‘Ÿ๐‘  ๐‘ฅ

โ‚ฑ 43.51

๐‘˜๐‘”= โ‚ฑ ๐Ÿ๐Ÿ,๐ŸŽ๐ŸŽ๐Ÿ,๐Ÿ๐Ÿ–๐Ÿ“.๐Ÿ—๐Ÿ“

Nitric Acid (55 % solution)

๐ถ = (13629.32 ๐‘˜๐‘”

๐‘‘๐‘Ž๐‘ฆ๐‘ฅ

1 ๐‘‘๐‘Ž๐‘ฆ

24 โ„Ž๐‘Ÿ๐‘ ) ๐‘ฅ 2400 โ„Ž๐‘Ÿ๐‘  ๐‘ฅ

โ‚ฑ 5.50

๐‘˜๐‘”= โ‚ฑ ๐Ÿ•,๐Ÿ’๐Ÿ—๐Ÿ”,๐Ÿ๐Ÿ๐Ÿ”

Dolomite

Page 14: Financial Analysis

Technological Institute of the Philippines

๐ถ = (431.1092 ๐‘˜๐‘”

๐‘‘๐‘Ž๐‘ฆ๐‘ฅ

1 ๐‘‘๐‘Ž๐‘ฆ

24 โ„Ž๐‘Ÿ๐‘ ) ๐‘ฅ 2400 โ„Ž๐‘Ÿ๐‘  ๐‘ฅ

โ‚ฑ2.07

๐‘˜๐‘”= โ‚ฑ ๐Ÿ–๐Ÿ—,๐Ÿ๐Ÿ‘๐Ÿ—.๐Ÿ”๐ŸŽ

Total Raw Materials Cost = 18,586,651.55

๐น๐‘–๐‘ฅ๐‘’๐‘‘ ๐ถ๐‘Ž๐‘๐‘–๐‘ก๐‘Ž๐‘™ ๐ถ๐‘œ๐‘ ๐‘ก๐‘  = ๐ท๐‘–๐‘Ÿ๐‘’๐‘๐‘ก ๐ถ๐‘œ๐‘ ๐‘ก + ๐ผ๐‘›๐‘‘๐‘–๐‘Ÿ๐‘’๐‘๐‘ก ๐ถ๐‘œ๐‘ ๐‘ก ๐‘ƒโ„Ž๐‘ = 174452504.8 + 155288784

๐‘ญ๐‘ช๐‘ช = โ‚ฑ๐Ÿ‘๐Ÿ๐Ÿ—๐Ÿ•๐Ÿ’๐Ÿ๐Ÿ๐Ÿ–๐Ÿ–.๐Ÿ–

๐‘‡๐‘œ๐‘ก๐‘Ž๐‘™ ๐ถ๐‘Ž๐‘๐‘–๐‘ก๐‘Ž๐‘™ ๐ถ๐‘œ๐‘ ๐‘ก = ๐น๐‘–๐‘ฅ๐‘’๐‘‘ ๐ถ๐‘Ž๐‘๐‘–๐‘ก๐‘Ž๐‘™ + ๐‘Š๐‘œ๐‘Ÿ๐‘˜๐‘–๐‘›๐‘” ๐ถ๐‘Ž๐‘๐‘–๐‘ก๐‘Ž๐‘™

= 329741288.8 +18,586,651.55

๐‘ป๐‘ช๐‘ช = โ‚ฑ ๐Ÿ‘๐Ÿ’๐Ÿ–๐Ÿ‘๐Ÿ๐Ÿ•๐Ÿ—๐Ÿ’๐ŸŽ.๐Ÿ’