1) What's the cost of a 700 KTA chlorine facility built in Mumbai, India given the following? - A chlorine plant with a 1025 KTA capacity was built in Orange, Texas in 2019 for a total of $985 M -The capacity factors to the right -$B = $A* ((capacity B/ capacity A)*) chlorine 0.45 SA=$ $8-$ 985,000,000 $Us 829,668,514 $US Capacity A= Capacity B= 1025 KTA 700 KTA 2) What's the cost of the same facility as described in question 1 given the following adjustments? The project expects an escalation factor of 2.35 from 2019 to 2028 -The project in Orange doesn't require piling like the project in Mumbai, so there is a $28MM deduction The project in India has a lower construction productivity due to monsoon season and restricted construction windows requiring a 1.20 modifier -The project in India is based upon a modular execution methodolgy, while the project in Orange was stick-built. The expected modifier in execution methodology difference is 0.80. -The government of India has created a new permit for projects that create byproducts of plastic. This will add 23% to the cost of the project in India. -Labor cost is cheaper in India, leading to a 20% deduction to the project cost. -Price after adjustments e= $A= $US $8 SUS Capacity A Capacity B KTA KTA <--New Price after adjustments <--New CFE after adjustments product capacity factors acolynitrile butadiene 0.6 0.68 0.45 ethanol 0.73 ethylene oxide 0.78 hydrochloric acid 0.68 hydrogen peroxide 0.75 methanol 0.6 nitric acid 0.6 phenol 0.75 polymerization 0.58 polypropylene 0.7 PVC 0.6 sulfuric acid 0.65 styrene 0.6 thermal cracking 0.7 urea 0.7 vinyl acetate 0.65 vinyl chloride 0.8 3) What's the dollar per KTA cost of the facility in India and the dollar per KTA cost of the facility in Orange? $USD/KTA Price of the facility in India $USD/ KTA Price of the facility in Orange 4) What's the cost of an LNG facility in Western Australia with all utility systems, acid gas removal, dehydration, mercury removal, LPG processing, and CO2 treatment given that the base facility was $680/MTPA? LNG Plant Type (4.5 MTPA Capacity) CAPEX Factor 1) Minimum feedgas treatment and imported utilities 2) Plant 1 plus all utility systems 1.00 1.25 3) Plant 2 plus acid gas removal, dehydration, mercury 1.64 4) Plant 3 plus LPG processing, storage, and loading 1.99 5) Plant 4 plus CO₂ treatment & sequestering 2.44 2.93 6) Plant 5 plus max LPG recovery and sulphur recovery SUSD/MTPA facility in Western Australia

Structural Analysis
6th Edition
ISBN:9781337630931
Author:KASSIMALI, Aslam.
Publisher:KASSIMALI, Aslam.
Chapter2: Loads On Structures
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Solve the questions below by typing in the correct factors or variables into the cells highlighted in orange and the right formulas into the cells highlighted in yellow.

- I completed question 1 but unsure about question 2 and 3.

1) What's the cost of a 700 KTA chlorine facility built in Mumbai, India given the following?
- A chlorine plant with a 1025 KTA capacity was built in Orange, Texas in 2019 for a total of $985 M
-The capacity factors to the right
-$B = $A* ((capacity B/ capacity A)*)
chlorine
0.45
SA=$
$8-$
985,000,000 $Us
829,668,514 $US
Capacity A=
Capacity B=
1025 KTA
700 KTA
2) What's the cost of the same facility as described in question 1 given the following adjustments?
The project expects an escalation factor of 2.35 from 2019 to 2028
-The project in Orange doesn't require piling like the project in Mumbai, so
there is a $28MM deduction
The project in India has a lower construction productivity due to monsoon
season and restricted construction windows requiring a 1.20 modifier
-The project in India is based upon a modular execution methodolgy, while the
project in Orange was stick-built. The expected modifier in execution methodology
difference is 0.80.
-The government of India has created a new permit for projects that create
byproducts of plastic. This will add 23% to the cost of the project in India.
-Labor cost is cheaper in India, leading to a 20% deduction to the project cost.
-Price after adjustments
e=
$A=
$US
$8
SUS
Capacity A
Capacity B
KTA
KTA
<--New Price after adjustments
<--New CFE after adjustments
product
capacity factors
acolynitrile
butadiene
0.6
0.68
0.45
ethanol
0.73
ethylene oxide
0.78
hydrochloric acid
0.68
hydrogen peroxide
0.75
methanol
0.6
nitric acid
0.6
phenol
0.75
polymerization
0.58
polypropylene
0.7
PVC
0.6
sulfuric acid
0.65
styrene
0.6
thermal cracking
0.7
urea
0.7
vinyl acetate
0.65
vinyl chloride
0.8
3) What's the dollar per KTA cost of the facility in India and the dollar per KTA cost of the facility in Orange?
$USD/KTA Price of the facility in India
$USD/ KTA Price of the facility in Orange
4) What's the cost of an LNG facility in Western Australia with all utility systems, acid gas removal, dehydration,
mercury removal, LPG processing, and CO2 treatment given that the base facility was $680/MTPA?
LNG Plant Type (4.5 MTPA Capacity)
CAPEX Factor
1) Minimum feedgas treatment and imported utilities
2) Plant 1 plus all utility systems
1.00
1.25
3) Plant 2 plus acid gas removal, dehydration, mercury
1.64
4) Plant 3 plus LPG processing, storage, and loading
1.99
5) Plant 4 plus CO₂ treatment & sequestering
2.44
2.93
6) Plant 5 plus max LPG recovery and sulphur recovery
SUSD/MTPA facility in Western Australia
Transcribed Image Text:1) What's the cost of a 700 KTA chlorine facility built in Mumbai, India given the following? - A chlorine plant with a 1025 KTA capacity was built in Orange, Texas in 2019 for a total of $985 M -The capacity factors to the right -$B = $A* ((capacity B/ capacity A)*) chlorine 0.45 SA=$ $8-$ 985,000,000 $Us 829,668,514 $US Capacity A= Capacity B= 1025 KTA 700 KTA 2) What's the cost of the same facility as described in question 1 given the following adjustments? The project expects an escalation factor of 2.35 from 2019 to 2028 -The project in Orange doesn't require piling like the project in Mumbai, so there is a $28MM deduction The project in India has a lower construction productivity due to monsoon season and restricted construction windows requiring a 1.20 modifier -The project in India is based upon a modular execution methodolgy, while the project in Orange was stick-built. The expected modifier in execution methodology difference is 0.80. -The government of India has created a new permit for projects that create byproducts of plastic. This will add 23% to the cost of the project in India. -Labor cost is cheaper in India, leading to a 20% deduction to the project cost. -Price after adjustments e= $A= $US $8 SUS Capacity A Capacity B KTA KTA <--New Price after adjustments <--New CFE after adjustments product capacity factors acolynitrile butadiene 0.6 0.68 0.45 ethanol 0.73 ethylene oxide 0.78 hydrochloric acid 0.68 hydrogen peroxide 0.75 methanol 0.6 nitric acid 0.6 phenol 0.75 polymerization 0.58 polypropylene 0.7 PVC 0.6 sulfuric acid 0.65 styrene 0.6 thermal cracking 0.7 urea 0.7 vinyl acetate 0.65 vinyl chloride 0.8 3) What's the dollar per KTA cost of the facility in India and the dollar per KTA cost of the facility in Orange? $USD/KTA Price of the facility in India $USD/ KTA Price of the facility in Orange 4) What's the cost of an LNG facility in Western Australia with all utility systems, acid gas removal, dehydration, mercury removal, LPG processing, and CO2 treatment given that the base facility was $680/MTPA? LNG Plant Type (4.5 MTPA Capacity) CAPEX Factor 1) Minimum feedgas treatment and imported utilities 2) Plant 1 plus all utility systems 1.00 1.25 3) Plant 2 plus acid gas removal, dehydration, mercury 1.64 4) Plant 3 plus LPG processing, storage, and loading 1.99 5) Plant 4 plus CO₂ treatment & sequestering 2.44 2.93 6) Plant 5 plus max LPG recovery and sulphur recovery SUSD/MTPA facility in Western Australia
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