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21
CHAPTER 2
MARKET ANALYSIS AND ECONOMIC
2.0 INTRODUCTION
Acrylonitrile was predominantly used for production of plastics such as acrylonitrile-
butadiene-styrene (ABS) and styrene-acrylonitrile (SAN), nitrile rubbers, nitrile barrier
resins, adiponitrile and acrylamide. On the other hand, the by-products produced in the
production of Acrylonitrile which are Acetonitrile and Hydrogen Cyanide (HCN), were
also studied to be fully utilized. The demand of Acrylonitrile is rising over the years and
consume by various industries over the world. Therefore, in order to design an
Acrylonitrile chemical plant, thorough analysis on the market and the economic sector
must be properly done. The study is also consists of estimation of the lost and profit of
running the industry.
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2.1 MARKET ANALYSIS
2.1.1 World Production of Acrylonitrile
According to Acrylonitrile and derivatives world supply/demand report 2009 done by
PCI Acrylonitrile Ltd. the acrylonitrile demand was increased in 2007 to reach the
highest total ever. However, in 2008 the demand is decreased due to the economic
problem. For the year of 2009, the demand and production of acrylonitrile is shown in
figure 2.1. World consumption of acrylonitrile is over 4 million tonnes. The USA is the
largest producer of acrylonitrile, with production of almost 2 million tonnes a year. Asia
is the largest consuming region of acrylonitrile, accounting for 39% of world
consumption, while production is growing fastest in North America. The USA and Japan
are the major exporters.
0
500
1000
1500
2000
2500
Th
ou
san
d T
on
s
Region
ACRYLONITRILE PRODUCTION AND
DEMAND
Demand
Production
Figure 2.1 Acrylonitrile Production and Demand (Garmston, S., 2009)
23
Table 2.1 Main country in Asia produces Acrylonitrile
COUNTRY
COMPANY/LOCATION
PRODUCTION
CAPACITIES
(TONS)
TOTAL
PRODUCTION
CAPACITIES
(TONS)
INDIA Reliance, Gujerat 50 000 50 000
SOUTH KOREA Tong Suh Petrochemical 300 000 550 000
Tae Kwang 250 000
TAIWAN CPDC 200 000 480 000
Formosa Plastics 280 000
THAILAND PTT Asahi Chemical Co
Ltd
2203 000 2203 000
CHINA Various company 2415 000 2415 000
(Garmston, S., 2009)
2.1.1.1 Forecast of Acrylonitrile Price and Demand
In this section, the production as well as the demand will be studied together for further
understanding the likelihood of the market balance to develop in the coming years. The
acrylonitrile supply and demand balance is forecast to improve over the upcoming
years. Thus, production of Acrylonitrile shows potential in attaining a profitable market.
Acrylonitrile demand growth is forecast to be increasing at 3.7% per year on
average for the period of 2008 - 2018. However, the forecast was a bit misleading as it
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starts from a very low base. Total demand of acrylonitrile in 2018 was expected to be
6.516 million tonnes. (World Supply/ Demand report, 2009)
A market trend of acrylic fibre which is one of the main sources of demand was
observed. In 2004, acrylic fibre has lost market share mainly to polyester due to its
relatively high price. The extensive use of fabrics woven from polyester thread or yarn
in apparel and home furnishing were also the main concern. In 2008, a substantial
volume of 520 000 tonnes of acrylic fibre were lost. However, growth of 127 000 tonnes
was seen as the volume regained in 2009. Therefore, we are expecting of more
acquisition in years to come.
Below are the graphs that show the forecasted production and demand of
acrylonitrile in year 2013 and 2018 by various parts of the world. We can see clearly
from both the graphs, production of acrylonitrile in Asia / Far East countries are
overwhelming. The production is targeted to exceed the demand. Therefore, it is a wise
decision to build acrylonitrile plant in any part of Asia to satisfy the needs of the
demands.
25
Figure 2.2 Production and demand of acrylonitrile in 2013
(Garmston, S., 2009)
Figure 2.3 Production and demand of acrylonitrile in 2018
(Garmston, S., 2009)
0
500
1000
1500
2000
2500
3000
3500
10
3to
nn
es
ACRYLONITRILE: PRODUCTION VS
DEMAND
2013
demand
production
0
500
1000
1500
2000
2500
3000
3500
4000
10
3to
nn
es
ACRYLONITRILE: PRODUCTION VS DEMAND
2018
demand
production
26
2.1.2 Raw Material
2.1.2.1 Propane
Table 2.2 Propane pricing
Propane (US dollar / Gallon)
Year Dec 2008 Dec 2009 Jul 2010
Prices $0.603 $1.318 $1.080
(Petronas Gas Berhad, 2010)
Table 2.2 shows the propane pricing from December 2008 till July 2010. From
the observation, it shows inconsistent price of propane from 2008 to 2010. The rapid
increase of propane from December 2008 to December 2009 proves that the demands
of propane is getting higher but slowly decrease in July 2010.
Table 2.3 Propane Demand
Company Country
Xinao Gas Hong Kong
Gail India India
Perusahaan Gas Negara Indonesia
S-Oil Corp South Korea
SUI Northern Gas
Pipeline
Pakistan
27
Petrochina Co. Singapore
Petronas Gas Malaysia Malaysia
(Petronas Gas Berhad, 2010)
Table 2.3 show the supplier of propane market in Asian. Primary suppliers in the
propane market include Xinao Gas (China), Gail India (India), Perusahaan Gas Negara
(Indonesia), S-Oil Corp (South Korea), SUI Northern Gas Pipeline (Pakistan),
Petrochina Co. (Singapore) and Petronas Gas Malaysia (Malaysia). (Petronas Gas
Berhad, 2010)
2.1.2.2 Ammonia
Ammonium hydroxide, also known as ammonia water, ammonical liquor, ammonia
liquor, aqua ammonia, aqueous ammonia, or simply ammonia, is a solution of ammonia
in water. It can be denoted by the symbols NH3(aq).
Table 2.4 Ammonia Purchase Price
Chemical compound
(Year)
Unit Size Unit Price (RM)
Ammonium Hydroxide
(2010)
500 ml 110.459
2.5 L 157.607
Ammonia, solution 32%,
reagent grade
(2008)
2.5 L 284.846
25 L 1,714.86
(Chem Supply Price List 2008 and Integra Chemical Catalog 2010)
28
Since the general economis crisis which heavily affected the downstream
fertilizer sector, as well as the reduces in industrial sector demand, ammonia prices has
drop $700-800/tonne from the peaks achieved in September 2008. In 2009, this
ammonia market is expected to change shape as a result of the dramatic fall in prices.
(The Market- Fertilizer News and Analysis, 2008)
Table 2.5 Ammonia Supplier in Asia Region
Company Country
Petronas Ammonia Sdn Bhd Malaysia
Pt. Kaltim Pasifik Amoniak Indonesia
Suzhou Industrial Park Yacoo Chemical
Reagent Co., Ltd.
Jiangsu, China
Shanghai Xunxin Chemical Co., Ltd Shanghai, China
Manus Aktteva Gujarat, India
Yongyi Chemicals Group Co., Ltd. Jiangsu, China
Jinan Haohua Industry Co., Ltd. Shandong, China
(www.chemicalregister.com, 2010)
From the Table 2.5, it shows that China is the largest ammonia manufacturer.
But, Pt. Kaltim Pasifik Amoniak which is located at Indonesia is one of the biggest
ammonia manufactures in the world.
29
2.1.2.3 Sulphuric acid
Table 2.6 Sulphuric acid purchase price
Sulphuric acid (RM / 500 ml)
Year January 2010
Prices RM 97.09
(Integra Chemical Catalog, 2010)
Table 2.6 shows the sulphuric acid pricing for years of 2010. According to ICIS
website, about 50 million tones of sulphuric acid was produced globally in 2009 over
90% being used in the production of sulphuric acid. It state that global prices of sulphur
and sulphuric was not stable starts in 2007 until 2008 driven by high demand in
industry. However, prices began to drop in the second half of 2008 in-line with the
global economic crisis and in late 2009, the demand in end use sectors improved
causing prices to rebound continuing into 2010. Compared to historical level prior to the
spike in 2007 and 2008, prices are currently at stable levels. At January 2010, the
prices start with the prices of RM 95.09 or US$ 30.34. (www.icis.com., 2009)
Table 2.7 Sulphuric acid major exporter and importer
Major Exporter Major Importer
Middle East China
Canada North Africa
Soviet Union India
United State
(Integra Chemical Catalogue, 2010)
30
Table 2.7 show the major exporter and importer of sulphuric acid around the
world. The major exporters were to Middle East, Canada and Soviet Union while the
major importer was India, United State, North Africa and China with 25% majority.
2.1.3 Catalyst
Table 2.8 Vanadium Catalyst purchase price
Vanadium Catalyst (RM / 500 ml)
Year January 2010
Prices RM 259.884
(Integra Chemical Catalogue, 2010)
Table 2.8 shows the vanadium catalyst pricing for year of 2010. Over the last 20
years, vanadium prices have shown a high degree of volatility. As experienced between
1998 and 2003, the price fall to the low but this does not happen in the economic
downturn in 2009. Many producers cut output and limited the fall in price. In mid 2010,
the recovery in price stalled for ferrovanadium. In long term forecast, the price will rise
reaching RM234.675/kg by 2015. Over the last decade, China has become both the
main producer and main consumer of vanadium. In terms of supply, it now accounts for
almost 50% of the global total and planned expansion over the next two years will
consolidate this position. Chinese demand for vanadium grew at 13%pa between 2003
and 2009.(www.roskill.com, 2009)
Table 2.9 Vanadium Catalyst Supplier
Company Country
Hebei Domydo Co., Ltd China
31
International Trading (IT) Limited United Kingdom
Angara Enterprise Ukraine
Highveld Steel & Vanadium Corp Witbank, South Africa
(www.alibaba.com)
Table 2.9 shows the supplier of vanadium catalyst around the world. Countries
with mature economies have much higher intensity of use of vanadium and in 2008,
intensity of use in USA was more than three times as great as that in China. Over the
next decade one of the main drivers for growth in vanadium demand will be a
combination of strong growth in steel output in Brazil, Russia, India and Canada
countries and an increasing emphasis n these countries on production of high strength
low alloy steels with their higher vanadium content. (www.roskill.com.,2009)
2.1.4 By-product Market Analysis
2.1.4.1 Acetonitrile
Acetonitrile is a co-product in the production of acrylonitrile and once purified, the
acetonitrile output is approximately 2.5-3% of acrylonitrile output and consequently the
acetonitrile supply/demand balance is totally governed by acrylonitrile output. There are
no commercial first intent producers of acetonitrile. As demand for acrylonitrile has
decreased owing to global economic slowdown, the production of acetonitrile has also
been decreased. A global shortage of acetonitrile is expected to remain the case well
into 2009.
Price for 1 tonne of acetonitrile = RM 6257.79 (HowTrade.com,2005)
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2.1.4.2 Hydrogen Cyanide (HCN)
Hydrogen cyanide forms in at least limited amounts from many combinations of
hydrogen, carbon, and ammonia. Hydrogen cyanide is currently produced in great
quantities by several processes, as well as being a recovered waste product from the
manufacture of acrylonitrile. Hydrogen cyanide is largely used in the production of other
chemicals. Its largest use is in the production of adiponitrile which in turn is used in the
production of nylon. The other uses are in the production of methyl methacrylate,
sodium cyanide, methionine, chelating agents, and cyanuric chloride (Mannsville
Chemical Product Synopsis July 1999, Chemical Market Reporter January 10, 2005).
The market for hydrogen cyanide is expected to grow slightly slower than the
GDP growth rate (Chemical Market Reporter January 10, 2005 and February 26, 2001;
Mannsville Chemical Product Synopsis July 1999). This analysis assumes that future
hydrogen cyanide supply will be within the range of 0.75 to 1 million tonnes per year.
2.4 ECONOMIC ANALYSIS
2.4.1 Fixed Capital Cost/ Investment
Fixed capital investment is amount of money needed to make the plat operable. Fixed
capital investment includes total cost of equipments, land cost, equipment installation
cost, etc. Table 2.3 shows the list of equipment needed for plant and estimation of its
cost.
33
Table 2.10 Number of major equipment according to type
Type of Equipment Number of
equipment
Price for 1 unit
(RM)
Price (RM)
Fluidized Bed
Reactor
1 459,773 459,773
Pump 5 200,000 1,000,000
Scrubber 1 119,504 119,504
Quench Column 1 282,744 282,744
Cooler 1 282,744 282,744
Heater 1 280,028 280,028
Distillation Column 3 1,650,000.00 4,950,000
Storage Tank 5 37,884 189,420
Compressor 1 214,368 214,368
Mixer 1 27,000 27,000
Total Equipment
Cost
20 7,805,581
(Source: http://matche.com and Perry, 1999)
Fixed capital investment consists of direct and indirect cost. Direct cost is cost
needed to install all the plant equipments and also for the surrounding of the plant but
for the indirect cost, it consists of all the legal activities and fees for contractors. Details
are shown in Table 2.4.
34
Table 2.11 Fixed Capital Investment of the Acrylonitrile Plant
Component Estimation Cost (RM) TOTAL
Direct Cost
Total Equipment Costs
7,805,581
Equipment Installation (includes
insulation and painting) 40% of total equipment cost 3,122,232.40
Piping System Installation 50% of total equipment cost 3,902,790.50
Instrumentation and Control 20% of total equipment cost 1,561,116.20
Electrical System Installation 15% of total equipment cost 1,170,837.15
Service facilities 50% of total equipment cost 3,902,790.50
Building, process and auxiliary 40% of total equipment cost 3,122,232.40
Land RM 30.00 per metre square
( 323,748.80 metre square) 9,712,464.00
Yard Improvement 12% of total equipment cost 936,669.72
TOTAL
35,236,714.00
Indirect Costs
Engineering and supervision 10% of total direct cost 3,523,671.40
Construction expenses 10% of total direct cost 3,523,671.40
Legal expenses 10% of total direct cost 3,523,671.40
Contractors fee 5% of total direct cost 1,761,835.70
Contingencies 12% of total direct cost 4,228,405.68
TOTAL
16,561,225.58
FIXED CAPITAL INVESTMENT Direct Costs + Indirect Costs
51,797,939.58
2.4.2 Operating Capital Cost
Raw materials, labor cost, catalyst cost, and Utilities cost plus fixed capital cost are the
needed for operating capital cost. Whereas, raw materials, labor, catalyst, and utilities
cost are the ingredients to make variable cost. All the calculations are shown below.
35
2.4.2.1 Annual Cost of Raw Materials
Table 2.12 Annual costs for Raw Material
Reactant tonne per year RM per tonne RM per year
Propane 96,360.00 1,409.09 135,779,912.40
Ammonia 74,460.00 915.39 68,159,939.40
Sulphuric Acid 185.84
TOTAL 203,939,851.80
2.4.2.2 Estimation of Operating Labor Cost
2.4.2.2.1 Operation Team
2.4.2.2.1.1 Shift Worker
Table 2.13 Shift Worker Cost
Position Quantity Salary/Month (RM) Total
Chemical Engineer 1 2,400.00 2,400.00
Shift Team Leader 1 1,750.00 1,750.00
Panel Boardmen 4 1,300.00 5,200.00
Process Field Operator 8 1,300.00 10,400.00
TOTAL 19,750.00
4 shifts = RM 19,750 x 4 = RM 79,000 (A)
2.4.2.2.1.2 Non-Shift Worker
Table 2.14 Non-Shift Worker Cost
Position Quantity Salary/Month (RM) Total
Safety Officer 2 2,200.00 4,400.00 (B)
36
2.4.2.2.2 Maintenance Team
Table 2.15 Maintenance Labor Cost
Position Quantity Salary/Month (RM) Total
Engineer 4 2,400.00 9,600.00
Technician 11 1,300.00 14,300.00
TOTAL 23,900.00 (C)
2.4.2.2.3 Additional Worker
Table 2.16 Additional Worker Cost
Position Quantity Salary/Month (RM) Total
Contractor 20 900.00 18,000.00
Guard 3 x 4 shifts 600.00 7,200.00
TOTAL 25,200.00 (D)
2.4.2.2.4 Administration Team
Table 2.17 Administration Worker Cost
Position Quantity Salary/Month (RM) Total
Human Resource Manager 1 1,750.00 1,750.00
Human Resource Staff 6 1,000.00 6,000.00
TOTAL 7,750.00 (E)
Total Labor Cost = A + B + C + D + E = RM 140,250 per month
= RM 1,683,000 per year
2.4.2.3 Catalyst Annual Cost
The catalyst used for production of acrylonitrile is vanadium catalyst
Table 2.18 Annual cost for catalyst
Reactant tonne per year RM per tonne RM per year
37
Vanadium 16.06 631.00 10,133.86
2.4.2.4 Estimation of Utilities Cost
Table 2.19 Estimation of Utilities Cost
Utilities Rate Quantity
Used TOTAL
Water
Water price :-
a) Industrial
Amount of water needed
for the first startup
RM 1.15 /m3 103 m3/day RM 118.45 /day
Total RM 42,405.00 /year
Electricity
electricity price :-
Tariff E1 Medium Voltage
General 6.6kV – 66kV
supply
RM 0.203
/kWh 5514.29 kWh
RM 1119.40 /day
Total power required RM 408,581.32 /year
Total utilities RM 450,986.32 / year
So, Total of Variable Cost =
= Raw Material + Labor Cost + Catalyst + Utilities
= RM 203,939,851.80 + RM 1,683,000 + RM 10,133.86+ RM 450,986.32
= RM 206,083,972.00 per year
Operating Cost = Fixed Capital + Variable Cost
= RM 51,797,939.58 + RM 206,083,972.00
= RM 257,881,911.60
38
2.4.3 Start-Up Costs
Start-up costs are the cost for the plant to start operating. Start-up costs will cover
process modifications, start-up labor, and loss in production. Estimation of start-up cost
is usually 10% from the fixed capital investment
Start-up Costs = 0.10 x fixed capital investment
= 0.10 x 51,797,939.58
= RM 5,179,793.96
2.4.4 Total Investment
Total capital investment = Operating capital investment + Start-up costs
= RM 257,881,911.60 + RM 5,179,793.96
= RM 263,061,705.60
2.4.5 Total Revenue
Table 2.20 Total Sales
Product tonne per year RM per tonne RM per year
Acrylonitrile 112,679.88 6,043.06 680,931,275.60
2.4.6 Break-Even Analysis
Contribution = selling price - variable cost
= RM 680,931,275.60 – RM 206,083,972.00
= RM 474,847,303.60
Breakeven Point = (fixed cost/ contribution) x selling price
= (RM 51,797,939.58 / RM 474,847,303.60) x
RM 680,931,275.60 /year
= RM 74,278,271.78 /year
39
Figure 2.4 Break-even analysis
2.4.7 Cash Flow Analysis
Table 2.21 Cash Flow
Variable Value (RM)
Cost Of Land 9,712,464.00
FCI 51,797,939.58
FCI1 25,898,969.79
FCI2 25,898,969.79
Working Capital 5,179,793.96
Yearly Sale Revenue 680,931,275.60
Cost Of Manufacturing 257,881,911.60
Salvage Value Plant 9,712,464.00
FCI = total investment
FCI1 = 50% from total investment for the first year
FCL2 = 50% from total investment for the second year
t = tax of government (15% in Terengganu)
40
Table 2.22 Rate of Return on Investment
End
Of
Year
(K)
Investment
Dk
FCI-dk
R
COMd
(R-COMd-
dk)*(1-t)+dk
Cash Flow
Cumulative
Cash Flow
0
9,712,464.00
51,797,939.58
0.00
-9,712,464.00
-9,712,464.00
1
25,898,969.79
51,797,939.58
0.00
-25,898,969.79
-35,611,433.79
2
25,898,969.79
51,797,939.58
0.00
-25,898,969.79
-61,510,403.58
3
10,359,587.92 41,438,351.66 680,931,275.60 206,083,972.00
405174146.2
405174146.2
343,663,742.67
4
16,575,340.67 24,863,010.99 680,931,275.60 206,083,972.00
406106509.2
406106509.2
749,770,251.83
5
9,945,204.40
14,917,806.59 680,931,275.60 206,083,972.00
405111988.7
405111988.7
1,154,882,240.55
6
5,967,122.64
8,950,683.95
680,931,275.60 206,083,972.00
404515276.5
404515276.5
1,559,397,517.00
7
5,967,122.64
2,983,561.31
680,931,275.60 206,083,972.00
404515276.5
404515276.5
1,963,912,793.46
8
2,983,561.31
0.00
680,931,275.60 206,083,972.00
404067742.3
404067742.3
2,367,980,535.72
9
680,931,275.60 206,083,972.00
403620208.1
403620208.1
2,771,600,743.78
10
680,931,275.60 206,083,972.00
403620208.1
403620208.1
3,175,220,951.84
11
680,931,275.60 206,083,972.00
403620208.1
403620208.1
3,578,841,159.90
12
-14,892,257.96
680,931,275.60 206,083,972.00
403620208.1
388727950.10
3,967,569,109.00
41
������� ���� = �
0 − 343,663,742.67
749,770,251.83 − 343,663,742.67=
� − 3
4− 3
� = 2.15 ��� !
Figure 2.4 Cumulative Cash Flow Diagram
2.5 CONCLUSION
From the research done, it is clear that, the demand of acrylonitrile is relatively high
especially in Asia countries. Therefore, the production of acrylonitrile will focus on
the Asia/Far East market.
This chemical plant producing acrylonitrile will be the first plant built in Asia.
Asia is the largest consuming region of acrylonitrile which accounts 39% of world
-100,000,000.00
0.00
100,000,000.00
200,000,000.00
300,000,000.00
400,000,000.00
500,000,000.00
600,000,000.00
700,000,000.00
800,000,000.00
0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20
Ca
sh F
low
(R
M)
Year
Cumulative Cash Flow Diagram
42
consumption. Therefore, it is a wise idea to produce acrylonitrile in order to cater the
demand of acrylonitrile.
As for the breakeven point, the sale that has to be made in one year is
actually lower that what the plant expected to sale. Hence it is clear that, the plant is
making profit every year.
From the market analysis, we know that, it takes about 2.15 years for the
company to get back its investment, which is generally very fast for a chemical
plant. Hence this is one of the advantages of this plant as it is very profitable.