Large LNG plant capabilities for capacity >2 MTPA Benefit ...
October 2014 2% $25.00 4% CERI Commodity Report ......LNG re-gasification capacity; while there were...
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bcf/d (BP, 2014). Therefore, the sum of all proposed LNG export projects in North America is 2.5 times greater than the total existing worldwide LNG trade, or roughly the equivalent of North America’s total natural gas consumption for 2013. As seen on Figure 1, almost half of this capacity is being planned in BC where proponents are looking for options to export low cost Western Canadian Sedimentary Basin (WCSB) natural gas to the more lucrative Asia-Pacific market where prices are much higher (Figure 2), and where it is estimated that 75% of global LNG demand occurred in 2013 (International Group of Liquefied Natural Gas Importers (GIIGNL), 2014). Figure 1: Planned and Existing LNG Export/Liquefaction Capacity in North America (MMtpa), by Region
Source: CERI
Figure 2: Global Natural Gas Prices ($/GJ), 2002-2014
Sources: (Alberta Energy, 2014), and (International Monetary Fund (IMF), 2014).
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US Gulf Coast (TX, LA, MS)
US West Coast (AK, OR)
US East Coast (GE, MD, ME)
Nova Scotia
Total Capacity: 645.8 MMtpa
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HENRY HUB @ USGC ($/GJ)
RUSSIAN GAS @ GERMANY ($/GJ)
INDONESIAN LNG @ JAPAN ($/GJ)
NORTH SEA BRENT @ EUROPE ($/GJ)
October 2014
CERI Commodity Report — Natural Gas
British Columbia (BC) Liquefied Natural Gas (LNG) Economics Carlos A. Murillo Recent media coverage around prospective LNG projects in BC has focused on the newly released LNG income tax and the LNG greenhouse gas (GHG) emissions’ benchmark proposed by the provincial government in late October. This article explores the impacts of these and other variables on the economics of a hypothetical LNG export (or liquefaction) facility located on the BC coast, targeting the Asia-Pacific LNG market. Various projects…maybe too many projects? According to the International Group of Liquefied Natural Gas Importers (GIIGNL) and the International Gas Union (IGU), total worldwide LNG trade in 2013 was estimated at 237 million tonnes (t) per year (MMtpa) or the equivalent of 32 bcf/d.1 It is also estimated that by year-end (YE) 2013 there were 29 importing countries with 104 receiving terminals and 721 MMtpa (96 bcf/d) of LNG re-gasification capacity; while there were 17 countries exporting LNG from 86 liquefaction trains with a total capacity of 286 MMtpa of LNG (38 bcf/d) (International Group of Liquefied Natural Gas Importers (GIIGNL), 2014) (International Gas Union (IGU), 2014). According to CERI’s research, the sum of all existing and proposed LNG export terminals in North America, a total of 51 separate projects, adds up to close to 646 MMtpa of capacity (or 86 bcf/d) (Figure 1). To further put that number into context, consider that estimates from the BP Statistical Review of World Energy indicate that natural gas consumption in North America (the United States, Canada, and Mexico, combined) in 2013 was 89
CERI Commodity Report – Natural Gas Editor-in-Chief: Dinara Millington ([email protected]) Contents Featured Article ................................................................................. 1 Natural Gas Prices.............................................................................. 7 Weather ............................................................................................ 9 Consumption and Production............................................................. 11 Transportation................................................................................... 13 Storage .............................................................................................. 15 Liquefied Natural Gas ........................................................................ 18 Drilling Activity .................................................................................. 16
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CERI’s analysis indicates that at most two large and one small LNG project off the BC coast will get built to serve the global LNG market. Not all projects will get built. Liquefaction facility capital costs (CAPEX): don’t let them run wild and free Compared to proposed projects in the US, most projects in BC, while having the advantage of being located in a cooler climate (lower operating costs) and closer to markets in the Asia-Pacific region (lower shipping distances and costs), will be built from scratch in remote areas where infrastructure is not as readily available (greenfield facilities). This compares to brownfield sites such as existing LNG re-gasification facilities and industrial clusters such as in the US Gulf Coast (USGC). This will generally translate into higher overall capital costs for BC projects. Capital costs, as will be discussed below, is in turn one of the most important considerations of the economics of an LNG (liquefaction) facility. While most projects in BC are at preliminary stages, CERI has gathered data on potential costs associated with various projects to be located on the West Coast of the continent, but primarily those in BC (Figure 3). The information was gathered from the project proponent’s websites, publicly available investor documents, and project description documents filed for export license purposes with the National Energy Board (NEB), as well as environmental impact assessments with the Canadian Environmental Assessment Agency (CEAA) and the BC Environmental Assessment Office (EAO). Figure 3: North American West Coast LNG Projects' Capital Cost Estimates ($/t)
Source: CERI Research
$395
$448
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$619
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$804
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$1,343
$- $200 $400 $600 $800 $1,000 $1,200 $1,400 $1,600
Douglas Channel Energy (BC LNG)
Kitimat LNG
Kitsault Energy
Oregon LNG
Pacific Northwest LNG
Prince Rupert LNG
Woodfibre LNG
Aurora
Steelhead LNG
Jordan Cove
Alaska South Central LNG
Woodside Energy LNG (Grassy Point LNG)
LNG Canada
$/t
As can be observed, these costs range from as little as $395/t of liquefaction capacity, to as much as $1,343/t of liquefaction capacity (with a weighted average of $859/t). Meanwhile, research conducted by Credit Suisse and the Oxford Institute for Energy Studies (OIES) indicates that the costs illustrated above could be conservative, as recent experience suggests that costs can be as high as over $2,000/t to over $3,000/t (Figure 4).2 This research also indicates, that in general, brand new facilities (like those being planned in BC) tend to have much higher costs than expansions/modifications of existing facilities or facilities to be developed on brownfield sites (such as those in the USGC). Figure 4: Recently Completed, Under Construction, and Planned LNG Project Costs
Source: (Ernst & Young (EY), 2013) after (Credit Suisse , 2012), and (Oxford Institute for Energy Studies (OIES), 2014)
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With a wide band of possible capital costs required for LNG liquefaction projects, this will be an important, if not the most important consideration with regard to LNG project economics for projects in BC. BC LNG economics example: tolling facility CERI has developed a model to better understand the different cost components of the LNG supply chain and their effects on the total project cost. This is a supply cost model based on the discounted cash flow (DCF) methodology which solves for the price required for a project proponent to recover all its costs (including capital costs, operating costs, and taxes) and earn a return on its investment (IRR=10% in the Base Case). In this case (Case 1), the example is for a hypothetical LNG tolling facility. The purpose of this facility is to take natural gas from a producer (at the LNG plant gate), liquefy it, and then load it onto a ship to be delivered to the end user. The shipping will be paid for by the buyer (freight on board (FOB)) or the seller (delivered ex-ship (DES)), depending on the sales agreement. Therefore, the supply cost which is being solved for in this model is the toll which is required to be charged by the liquefaction facility owner in order to recover all of its costs and receive a return on its investment. Alternatively, if this was an integrated project where the project proponent owns natural gas reserves, natural gas transmission, and liquefaction facilities, the supply cost solved for by this model, will be the equivalent to the liquefaction costs portion of the total integrated project’s LNG supply costs. In summary, for a tolling facility the results of this analysis are the required toll to be charged, while for an integrated project the resulting costs reflect the liquefaction costs of the integrated LNG project.
Table 1 displays the main assumptions used in this model while Figure 5 and Table 2 display the results for the base case. Table 1: Model Assumptions
Figure 5: Liquefaction Costs/Toll by Component
Hypothetical BC LNG Facility
Train Capacity 6 MMtpa 801 MMcf/d
Number of Trains 3 #
Total Capacity 18 MMtpa 2,402 MMcf/d
CAPEX $ 859 $/t
Project's CAPEX $ 15,458 $MM
Construction Time 5 Years
Decommisioning Costs $ 1,546 $MM
Foreign Expenditure = USD % of Capex 54% % of Total
Facility Fixed OPEX $ 0.54 $/mcf
Pipeline Transportation Costs $ 0.50 $/mcf
Project's GHG Intensity 0.22 t CO2 eq./t LNG
Liquefaction Portion GHG Intensity 0.10 t CO2 eq./t LNG
BC LNG Emissions Benchmark 0.16 t CO2 eq./t LNG
mcf of gas for PG/mcf of LNG 0.04
Estimated Gas Treating Shrinkage Vol. 5% of input volume
CAPEX Inflation 3.5% %/yr
OPEX Inflation 2.5% %/yr
Price Inflation 2.0% %/yr
Discount Rate (DR) 10.00% %
CAD/USD 1.10 $CAD/$US
Federal Corporate Tax Rate 15% %
Provincial Corporate Tax Rate 11% %
Natural Gas Carbon Tax Rate $ 1.6 $/mcf
Carbon Tax $ 30.0 $/t
BC LNG Income Tax Structure
Pre-Payout 1.5% %
Post-Payout 3.5% %
Post-Payout after 2037 5.0% %
Wegithed Avg. Depreciation Rate (LNG Plant: Class 47) 14.8% %
Alernative Wegithed Avg. Depreciation Rate (LNG Plant: Class 43) 24.1% %
Gas Heating Value 1.09 GJ/mcf 22.50 GJ/t of LNG
WCSB Gas Price AECO-C $ 3.50 $/GJ
WCSB Gas Price AECO-C $ 3.82 $/mcf
Taxation
Prices
BC LNG ECONOMICS: CASE 1: TOLLING FACILITY
Project Description
Project's Costs
Inflation/Return/Exchange Rates
61%
17%
11%8%
1%2%
Capital Costs
LNG Facility Fixed OPEX
LNG Facility Var OPEX
Corporate Taxes
LNG Income Taxes
Carbon Taxes
Total Costs ($/GJ): $6.51
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Table 2: Base Case Results
The results indicate that an 18 MMtpa facility with a weighted average CAPEX of $859/t – assuming construction occurs starting in 2014-2015, with first LNG in 2018 and decommissioning by 2047 – will require a toll of $6.51/GJ (in real $2014) over the project’s life to obtain an internal rate of return (IRR) of 10 percent.3 This analysis also indicates that capital costs account for 61% of the total project cost, compared to 28% for operating costs (fixed plus variable), and 11% for all forms of taxes combined (including federal and provincial corporate income taxes, carbon taxes, and the LNG income tax). For an integrated project – assuming a dry-gas supply cost of about $2.4/GJ4 for a producer in the Montney area, a $1.0/GJ processing and transportation fee from the field to liquefaction facility, and a $1.3/GJ shipping cost to the Asia-Pacific market – this will result in total delivered LNG supply costs of $11.2/GJ today.5 Alternatively, if this was a merchant facility where the LNG facility owner would buy feed gas at the local market price/pool (AECO-C/Station 2) and cover all the other costs, assuming a $3.50/GJ AECO-C/Station 2 price (2013-14 (J-A) avg.), the delivered LNG price would be $12.3/GJ today.6 These examples show that the liquefaction costs will remain the single largest cost component of an LNG project across any of the different supply chain cases. Given that capital costs account for over half of the total liquefaction costs,7 this implies that having strong controls on these costs will be very important for the success and economic viability of LNG projects in BC.
Discounted ($2014)
LNG Output (GJ) 3,232,051,506.44
($MM) $/GJ $/mcf % of Total
Tolling Revenues $ 21,025 $ 6.51 $ 7.10 100.0%
Capital Costs $ 12,746 $ 3.94 $ 4.30 60.6%
LNG Facility Fixed OPEX $ 3,596 $ 1.11 $ 1.21 17.1%
LNG Facility Var OPEX $ 2,298 $ 0.71 $ 0.78 10.9%
Corporate Taxes $ 1,630 $ 0.50 $ 0.55 7.8%
LNG Income Taxes $ 330 $ 0.10 $ 0.11 1.6%
Carbon Taxes $ 425 $ 0.13 $ 0.14 2.0%
NCF $ (0) $ (0.00) $ (0.00) 0.0%
Total Costs $ 21,025 $ 6.51 $ 7.10 100.0%
Capital Costs $ 12,746 $ 3.94 $ 4.30 60.6%
Operating Costs $ 5,893 $ 1.82 $ 1.99 28.0%
Taxes $ 2,386 $ 0.74 $ 0.81 11.3%
Total Costs $ 21,025 $ 6.51 $ 7.10 100.0%
Model Results: Base Case
Don’t be so sensitive capital: sensitivity analysis Table 3 displays the result of a sensitivity analysis on the different variables used in the model and their effect on the resulting facility toll/liquefaction costs. Table 3: Sensitivity Analysis
As can be observed, the capital costs of the facility have the highest effect on the project’s economics when using our toll/liquefaction supply costs metric. As an example, using a $1,343/t CAPEX instead of $859/t (or a 56% increase in CAPEX) results in a 39% increase in the required toll/liquefaction costs pushing the toll up to $9.07/GJ. On the other hand, a $395/t capital cost (or a 54% reduction from the $859/t base case) results in a 38% decrease in the facility required toll at $4.07/GJ. This also indicates that for every 1% change in capital expenditures, the required toll will change by 0.70% (% change in toll/% change in variable = elasticity). Thus the higher the toll/variable’s elasticity, the larger the impact of the variable in question on the required toll. After capital costs, the most important variables include the exchange rate and the discount rate, followed by fixed operating costs, and variable operating costs. Surprisingly, the least sensitive variables, as seen on Table 3, are the LNG income tax rate and the applied capital cost allowance (CCA) depreciation rate. In regard to the LNG income tax rate, while there is no question that different taxation rates will result in different total amounts of tax paid on an annual and a cumulative basis, the sensitivity analysis indicates that to
CAPITAL COSTSVariable % Change from
Base CaseToll ($/GJ)
Toll %
Change
From Base
Case
Toll/Variable Elasticity
= % chg. In Toll/% chg.
In Var.
CAPEX Base Case $ 859 $/t 0.0% $ 6.51 0.0% n/a
High CAPEX $ 1,343 $/t 56.3% $ 9.07 39.4% 0.70
Low CAPEX $ 395 $/t -54.0% $ 4.07 -37.5% 0.70
EXCHANGE RATE
Exchange Rate Case Case 1.10 CAD/USD 0.0% $ 6.51 0.0% n/a
High Exchange Rate 1.21 CAD/USD 10.0% $ 6.76 3.9% 0.39
Low Exchange Rate 0.99 CAD/USD -10.0% $ 6.25 -3.9% 0.39
DISCOUNT RATE
Discount Rate Base Case 10.0% % 0.0% $ 6.51 0.0% n/a
High Discount Rate 12.5% % 25.0% $ 6.94 6.8% 0.27
Low Discount Rate 7.5% % -25.0% $ 6.14 -5.6% 0.23
OPERATING COSTS
Fixed OPEX
Fixed OPEX Base Case $ 0.54 $/mcf 0.0% $ 6.51 0.0% n/a
High Fixed OPEX $ 0.68 $/mcf 25.0% $ 6.78 4.3% 0.17
Low Fixed OPEX $ 0.41 $/mcf -25.0% $ 6.23 -4.3% 0.17
Variable OPEX
Var. OPEX Base Case (AECO Price) $ 3.50 $/GJ 0.0% $ 6.51 0.0% n/a
High Var. OPEX $ 4.38 $/GJ 25.0% $ 6.68 2.7% 0.11
Low Var. OPEX $ 2.63 $/GJ -25.0% $ 6.33 -2.7% 0.11
TAXES
LNG Income Tax Rate
Post-Payout Base Case 1.5% -->3.5% -->5.0% % 0.0% $ 6.51 0.0% n/a
Post-Payout High Case 3.5% -->5.5% -->7.0% % 42.9% $ 6.63 2.0% 0.05
Post-Payout Low Case 0.0% -->2.0% -->3.5% % -42.9% $ 6.44 -1.0% 0.02
Depreciation Rate
W.AV Dep. Rate CCA Class 47 14.8% % 0.0% $ 6.51 0.0% n/a
W.AV Dep. Rate CCA Class 43 24.1% % 62.3% $ 6.47 -0.6% (0.01)
Sensitivity Analysis
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compensate for those higher or lower rates, the tolls/liquefaction costs would need to change minimally. As an example, a lower LNG income tax rate of 2.0% post-payout (and 3.5% post-payout after 2037) would result in a 1.0% (or $0.06/GJ) decrease in the toll/liquefaction costs. Meanwhile, an increase in the tax rate (5.5% post-payout and 7.0% after 2037) will require the toll to be higher by 2.0% (or by $0.13/GJ). When we consider different CCA rates,8 a higher CCA rate allows for the owner of the facility to depreciate its equipment/assets faster and thus re-invest their capital. Thus, on an annual cash-flow basis, the impact of different CCA rates would be more pronounced, and be reflected in the project’s rate of return. Yet under both circumstances only 100% of the capital is depreciated. This means that different depreciation rates result in a shift in the tax burden over time with a higher depreciation rate indicating that there are more tax deductions for the project proponent on the earlier years of the project and less tax deductions later on (which from the project owner’s perspective means that they can recover their money faster for re-investment purposes). The opposite is true for a lower depreciation rate, however the overall deduction is the same in both cases (100%). In this analysis, given the long-term nature of the project (34 years from construction to decommissioning), and given that the costs are discounted over such a long-term timeframe, it is reasonable to expect that different CCA rates would have a small impact on the resulting toll as seen in the sensitivity analysis. And, so we conclude Recently we have heard analogies alluding to the BC provincial government killing the goose before it lays the golden egg with their fiscal regime. Fiscal terms and government take, while controversial, do not appear to have a significant impact on project economics (when using our developed LNG supply cost metric). Our analysis indicates that the golden goose perhaps needs to focus more on other aspects of their projects.
Our model suggests that the key make or break issue surrounding these projects is around capital costs, followed by exchange rates, discount rates, and operating costs. Exchange rates and variable operating costs will largely be driven by commodity prices, macro-economic factors, and overall market conditions, and thus are generally beyond the proponents’ control. The onus will then fall on the project proponents’ ability to manage capital costs (or to adjust their expectations on returns (discount rates)). Managing projects’ costs, however, has proven to be a difficult task in other instances where oil and gas mega-projects have been built with large cost overruns.9 Lessons from those experiences need to be applied to prospective LNG projects in BC for them to be successful. Successful companies will need to enforce strong cost controls during the construction phase. Long-term sales contracts with end-users will also be key in getting assurance on LNG prices in order to drive final investment decisions (FIDs), which we have yet to hear about in regards to BC LNG projects. And while project costs are important, LNG buyers will also benefit from supply diversification by investing in and purchasing output from Canadian LNG projects. Without a doubt, there are numerous challenges ahead for proponents of BC LNG projects. Yet identifying those challenges is the first step in dealing with them. In the meantime, CERI will continue to monitor and analyze energy and environmental issues that affect Canadian producers and consumers. Endnotes 1Using a conversion factor of 48.7 mcf of natural gas per tonne of LNG 2It is important to note that both sets of costs are not always comparable as the costs for the projects in North America are generally associated with the liquefaction and export facilities while some of the estimates for other projects around the world might include upstream and midstream (transportation and processing) costs in addition to the liquefaction and export facilities. Some project costs also include additional infrastructure costs such as for carbon dioxide injection (as in the case with Gorgon (NW Australia) and Snohvit (Norway)) 3Other recently developed estimates by Macquarie and the International Energy Agency (IEA) suggest the liquefaction
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costs for Canadian LNG projects to be around $5/GJ to $6/GJ. See: (International Energy Agency (IEA), 2014), and (Macquarie Private Wealth , 2012) 4See: (Dalzell, 2013), Page 30 5Alternatively, if the original DCF analysis is extended to include the upstream and midstream components of an integrated project (plus shipping), the resulting supply costs (which are equal to the market price required in the Asia-Pacific for the producer to recover all costs plus a 10% after-tax rate of return) are calculated to be $14.9/GJ. This compares to about $14/GJ for Canadian LNG projects as estimated by the IEA. See Figure 2.24, Page 114 (International Energy Agency (IEA), 2014). 6This is similar to the Cheniere Energy model for its Sabine Pass and Corpus Christi facilities in the USGC. See: (Bloomberg Businessweek, 2014) and www.cheniere.com. Assuming a $4.5/GJ Henry Hub price, a $0.4/GJ pipeline toll, a $3.6/GJ liquefaction toll, and a shipping cost of $2.8/GJ to the Asia-Pacific market, the comparable landed price from a Gulf Coast facility like Cheniere’s would be $11.3/GJ today. 7Meanwhile, labour costs can account for about 1/3 or more of the total capital costs: See: (Oxford Institute for Energy Studies (OIES), 2014), and (KBR, n/a) 8Weighted average CCA rates are used in this model because the LNG liquefaction project will have different types of assets which will be depreciated at different rates 9These include oil sands projects in northeastern Alberta, LNG projects in Australia, and other specific examples such as development of the Kashagan oil field in the Caspian Sea, and the Escravos GTL facility in Nigeria, among others References Alberta Energy. (2014). Monthly Reference Price Calculations.
Retrieved from Alberta Energy: http://energy.alberta.ca/NaturalGas/1316.asp
Bloomberg Businessweek. (2014, November 6). Energy - US Natural Gas Exports Will Fire Up in 2015. Retrieved from Bloomberg Businessweek - Energy: http://www.businessweek.com/articles/2014-11-06/u-dot-s-dot-natural-gas-exports-will-fire-up-in-2015
BP. (2014). BP. Retrieved from BP Statistical Review of World Energy 2014: http://www.bp.com/en/global/corporate/about-bp/energy-economics/statistical-review-of-world-energy.html
Alberta Energy. (2014). Monthly Reference Price Calculations. Retrieved from Alberta Energy: http://energy.alberta.ca/NaturalGas/1316.asp
Bloomberg Businessweek. (2014, November 6). Energy - US Natural Gas Exports Will Fire Up in 2015. Retrieved from Bloomberg Businessweek - Energy: http://www.businessweek.com/articles/2014-11-06/u-dot-s-dot-natural-gas-exports-will-fire-up-in-2015
BP. (2014). BP. Retrieved from BP Statistical Review of World Energy 2014: http://www.bp.com/en/global/corporate/about-bp/energy-economics/statistical-review-of-world-energy.html
Credit Suisse . (2012, June 07). Global LNG Sector - Update . Retrieved from Credit Suisse, Global Equity Research : https://research-and-analytics.csfb.com/docView?language=ENG&format=PDF&document_id=977153251&source_id=em&serialid=lLnIHOuVvGf%2BeB6YKN9IA%2Bot%2FumB3JhDoxYEUUEK08s%3D
Dalzell, J. (2013, December). Conventional Natural Gas Supply Costs in Western Canada - An Update . Retrieved from Canadian Energy Research Institute (CERI): http://ceri.ca/images/stories/2013-12-17_CERI_Study_136__Update_Conventional_Natural_Gas_Supply_Costs.pdf
Ernst & Young (EY). (2013). Global LNG: Will new demand and new supply mean new pricing? Retrieved from Ernst & Young (EY): http://www.ey.com/Publication/vwLUAssets/Global_LNG_New_pricing_ahead/$FILE/Global_LNG_New_pricing_ahead_DW0240.pdf
International Energy Agency (IEA). (2014, November). Africa Energy Outlook - World Energy Outlook (WEO) Special Report . Retrieved from International Energy Agency (IEA): http://www.iea.org/publications/freepublications/publication/WEO2014_AfricaEnergyOutlook.pdf
International Gas Union (IGU). (2014). IGU World LNG Report - 2014 Edition. Retrieved from International Gas Union (IGU): http://www.igu.org/sites/default/files/node-page-field_file/IGU%20-%20World%20LNG%20Report%20-%202014%20Edition.pdf
International Group of Liquefied Natural Gas Importers (GIIGNL). (2014). The LNG Industry in 2013. Retrieved from International Group of Liquefied Natural Gas Importers (GIIGNL): http://www.giignl.org/sites/default/files/PUBLIC_AREA/Publications/giignl_the_lng_industry_fv.pdf
International Monetary Fund (IMF). (2014). IMF Primary Commodity Prices . Retrieved from International Monetary Fund (IMF): http://www.imf.org/external/np/res/commod/index.aspx
KBR. (n/a). LNG Liquefaction - Not All Plants Are Created Equal. Retrieved from KBR: http://www.kbr.com/Newsroom/Publications/Technical-Papers/LNG-Liquefaction-Not-All-Plants-Are-Created-Equal.pdf
Macquarie Private Wealth . (2012, September 10). Canadian LNG: The race to the coast - Our views on Canadian LNG. Retrieved from Macquarie Private Wealth : http://www.investorvillage.com/uploads/8056/files/Cdn_LNG_100912.pdf
Oxford Institute for Energy Studies (OIES). (2014, February). LNG Plant Cost Escalation. Retrieved from Oxford Institute for Energy Studies (OIES): http://www.oxfordenergy.org/wpcms/wp-content/uploads/2014/02/NG-83.pdf
US Energy Information Administration (EIA). (2014). Natural Gas Spot and Future Prices (NYMEX). Retrieved from US Energy Information Administration (EIA): http://www.eia.gov/dnav/ng/ng_pri_fut_s1_d.htm
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-11
Ju
l-12
Jan
-14
Dif
fere
nti
al
He
nry
Hu
bC
hic
ag
o
He
nry H
ub
/C
hic
ag
o
Beginning of N
ext M
onth S
pot P
rice (U
S$/M
MB
tu)
CERI Commodity Report - Natural Gas
Page 8
SOU
RC
E: C
anad
ian
Gas
Ass
oci
atio
n.
SOU
RC
E: C
ERI,
Can
adia
n G
as A
sso
ciati
on
, Sta
tisti
cs C
anad
a.
SOU
RC
E: N
OA
A.
SOU
RC
E: C
ERI,
NO
AA
, EIA
.
0
100
200
300
400
50
0
60
0
70
0
80
0
JF
MA
MJ
JA
SO
ND
5-Y
ear
Avg
.20
13
20
14
Ca
na
dia
n H
ea
tin
g D
eg
re
e D
ays
0
100
200
300
400
500
600
700
800
900
1,0
00
JF
MA
MJ
JA
SO
ND
5-Y
ear
Avg
.20
13
20
14
US
H
ea
tin
g D
eg
re
e D
ays
01234567
0
20
0
40
0
600
800
1,0
00
1,2
00 J
an
-09
Jan
-10
Jan
-11
Jan
-12
Jan
-13
Jan
-14
Deg
ree D
ay
sC
on
su
mp
tio
n
Ca
na
dia
n H
eatin
g D
eg
re
e D
ays vs R
esid
en
tia
l a
nd
Co
mm
erc
ia
l C
on
su
mptio
n
Deg
ree D
ays
BC
FP
D 010
20
30
40
50
60
0
200
40
0
600
800
1,0
00
1,2
00 J
an
-09
Jan
-10
Jan
-11
Jan
-12
Jan
-13
Jan
-14
Deg
ree D
ay
sC
on
su
mp
tio
n
US
H
ea
tin
g D
eg
re
e D
ays vs
Re
sid
en
tia
l a
nd
C
om
me
rc
ia
l C
on
su
mp
tio
n
Deg
ree D
ays
BC
FP
D
Relevant • Independent • Objective
Page 9
SOU
RC
E: E
nvi
ron
men
t C
anad
a.
SOU
RC
E: E
nvi
ron
men
t C
anad
a.
SOU
RC
E: N
OA
A.
SOU
RC
E: N
OA
A.
CERI Commodity Report - Natural Gas
Page 10
SOU
RC
E: N
OA
A.
SOU
RC
E: E
nvi
ron
men
t C
anad
a.
SOU
RC
E: N
OA
A.
Relevant • Independent • Objective
Page 11
SOU
RC
E: S
tati
stics
Can
ada.
SO
UR
CE:
Sta
tisti
cs C
anad
a, N
EB.
SOU
RC
E: E
IA.
SOU
RC
E: E
IA.
02468
10
12
14
16 J
an
-09
Jan
-10
Ja
n-1
1J
an
-12
Jan
-13
Ja
n-1
4
Ind
ustr
ial
& P
ow
er
Co
mm
erc
ial
Res
ide
nti
al
Ca
na
dia
n C
on
su
mp
tio
n
By S
ector (B
cfp
d)
02468
10
12
14
16
18
20 J
an
-09
Jan
-10
Jan
-11
Jan
-12
Jan
-13
Jan
-14
BC
, Y
uko
n,
NW
TA
BS
KE
. C
oas
t
Ca
na
dia
n M
arke
ta
ble
P
ro
du
ctio
n
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ro
vin
ce
/R
eg
io
n (B
cfp
d)
0
20
40
60
80
10
0
12
0
14
0 Jan
-09
Jan
-10
Jan
-11
Jan
-12
Jan
-13
Jan
-14
Ind
ustr
ial
Ele
ctr
ic P
ow
er
Co
mm
erc
ial
Res
ide
nti
al
US
C
on
su
mp
tio
n
By S
ec
tor (B
cfp
d)
0
10
20
30
40
50
60
70
80 J
an
-09
Jan
-10
Jan
-11
Jan
-12
Jan
-13
Jan
-14
US
To
tal
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uis
ian
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era
l W
ate
rsT
ex
as
US
M
ark
eta
ble
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ro
du
ctio
n (B
cfp
d)
CERI Commodity Report - Natural Gas
Page 12
SOU
RC
E: S
tati
stics
Can
ada,
NEB
. SO
UR
CE:
Sta
tisti
cs C
anad
a, N
EB.
SOU
RC
E: S
tati
stics
Can
ada,
NEB
. SO
UR
CE:
Sta
tisti
cs C
anad
a, N
EB.
0.0
1.0
2.0
3.0
4.0
5.0
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MJ
JA
SO
ND
20
12
20
13
20
14
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, Y
uk
on
, N
WT
M
ark
eta
ble
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ro
du
ctio
n (B
cfp
d)
02468
10
12
14
16
JF
MA
MJ
JA
SO
ND
20
12
20
13
20
14
Alb
erta
M
ark
eta
ble
P
ro
du
ctio
n (B
cfp
d)
0.0
0.5
1.0
JF
MA
MJ
JA
SO
ND
20
12
20
13
20
14
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sk
atc
he
wan M
arke
ta
ble
P
ro
du
ctio
n (B
cfp
d)
0.0
0
0.2
5
0.5
0
JF
MA
MJ
JA
SO
ND
20
12
20
13
20
14
Ea
st C
oa
st M
ark
eta
ble
P
ro
du
ctio
n (B
cfp
d)
Relevant • Independent • Objective
Page 13
SOU
RC
E: C
ERI.
SO
UR
CE:
CER
I.
SOU
RC
E: N
EB.
SOU
RC
E: N
EB.
02468
10
12
14
16
JF
MA
MJ
JA
SO
ND
20
12
20
13
20
14
Syste
m F
ie
ld
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ec
eip
ts
Tra
nsC
an
ad
a +
W
estc
oa
st; M
on
th
ly A
ve
ra
ge
(B
cfp
d)
02468
10
12
14
16
Oct-
13
Dec-1
3F
eb
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r-14
Ju
n-1
4A
ug
-14
Oct-
14
Em
pre
ss
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Ne
ill
AB
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All
ian
ce
Alb
erta
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yste
m D
elive
rie
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cfp
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p-1
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ov-1
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an
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ay-1
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14
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gs
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e U
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oin
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est (B
cfp
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as E
xp
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th
e U
S
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xp
ort P
oin
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cfp
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CERI Commodity Report - Natural Gas
Page 14
SOU
RC
E: N
EB.
SOU
RC
E: N
EB.
SOU
RC
E: N
EB, E
IA.
SOU
RC
E: N
EB.
02468
10
12
Se
p-1
3N
ov-1
3J
an
-14
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r-1
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ay-1
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14
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p-1
4
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st
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st
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st
US
Im
po
rts o
f C
an
ad
ia
n G
as
By U
S R
eg
io
n (B
cfp
d)
02468
10
12
14
16
18
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ay
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st
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io
n (C
$/G
J)
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an
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ay
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urt
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cfp
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12
14 Au
g-1
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13
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ad
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exic
o
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ta
l U
S P
ip
elin
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as Im
po
rts (B
cfp
d)
Relevant • Independent • Objective
Page 15
SOU
RC
E: C
ERI,
Pla
tts
Gas
Dai
ly.
SOU
RC
E: C
ERI,
Pla
tts
Gas
Dai
ly.
SOU
RC
E: C
ERI,
Pla
tts
Gas
Dai
ly.
SOU
RC
E: C
ERI,
Pla
tts
Gas
Dai
ly.
0
100
200
300
40
0
500
600
70
0
80
0
900
1,0
00
JF
MA
MJ
JA
SO
ND
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r A
vg
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32
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dia
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ra
ge
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cf, M
on
th
-e
nd
)
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500
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00
1,5
00
2,0
00
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00
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00
3,5
00
4,0
00
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00
Oct-
13
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n-1
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ug
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14
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st
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st
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du
cin
g R
eg
ion
US
S
torage by R
egion (B
cf, M
onth-end)
0
500
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00
1,5
00
2,0
00
2,5
00
3,0
00
3,5
00
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00
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00
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ow
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0
20
0
300
400
50
0
600
700
80
0
900
Oct-
13
Dec-1
3F
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Ap
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Ju
n-1
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ug
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Oct-
14
West
Ea
st
Canadian S
torage by R
egion (B
cf, M
onth
-end)
CERI Commodity Report - Natural Gas
Page 16
SOU
RC
E: C
ERI,
Pla
tts
Gas
Dai
ly.
SOU
RC
E: C
ERI,
Pla
tts
Gas
Dai
ly.
SOU
RC
E: C
ERI,
Pla
tts
Gas
Dai
ly.
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-120
-100
-80
-60
-40
-200
20
40
60
JF
MA
MJ
JA
SO
ND
WC
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D
5-Y
ear
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13
20
14
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ste
rn
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an
ad
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to
ra
ge
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je
ctio
ns/W
ith
dra
wals
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cf, M
on
th
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nd
)
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-200
-150
-100
-500
50
100
150
JF
MA
MJ
JA
SO
ND
5-Y
ear
Avg
.20
13
20
14
Canadian S
torage
Injections/W
ithdraw
als (B
cf, M
onth
-end)
-100
-80
-60
-40
-200
20
40
60
80
JF
MA
MJ
JA
SO
ND
5-Y
ear
Avg
.20
13
20
14
Eastern C
anadian S
torage Injections/W
ithdraw
als
(B
cf, M
onth-end)
Relevant • Independent • Objective
Page 17
SOU
RC
E: C
ERI,
Pla
tts
Gas
Dai
ly.
SOU
RC
E: C
ERI,
Pla
tts
Gas
Dai
ly.
SOU
RC
E: C
ERI,
Pla
tts
Gas
Dai
ly.
SOU
RC
E: C
ERI,
Pla
tts
Gas
Dai
ly.
-150
-100
-500
50
100
JF
MA
MJ
JA
SO
ND
5-Y
ear
Avg
.20
13
20
14
US
W
estern C
onsum
ing R
egion S
torage
Injections/W
ithdraw
als (B
cf, M
onth
-end)
-400
-300
-200
-1000
100
200
JF
MA
MJ
JA
SO
ND
5-Y
ear
Avg
.20
13
20
14
US
P
roducing R
egion S
torage Injections/W
ithdraw
als
(B
cf, M
onth-end)
-1200
-1000
-800
-600
-400
-2000
200
400
600
800
JF
MA
MJ
JA
SO
ND
5-Y
ear
Avg
.20
13
20
14
US
S
torage
Injections/W
ithdraw
als (B
cf, M
onth
-end)
-700
-500
-300
-100
100
300
500
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MA
MJ
JA
SO
ND
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ear
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13
20
14
US
E
astern S
torage
Injections/W
ithdraw
als (B
cf, M
onth
-end)
CERI Commodity Report - Natural Gas
Page 18
SOU
RC
E: U
S D
OE.
SO
UR
CE:
US
DO
E.
SOU
RC
E: U
S D
OE.
SO
UR
CE:
US
DO
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ility (B
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rice (U
S$/M
MB
tu)
Relevant • Independent • Objective
Page 19
SOU
RC
E: U
S D
OE,
NEB
. SO
UR
CE:
US
DO
E.
SOU
RC
E: E
IA, U
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cf)
CERI Commodity Report - Natural Gas
Page 20
SOU
RC
E: C
ERI,
CA
OD
C, B
aker
Hu
ghes
. SO
UR
CE:
CER
I, C
AO
DC
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SOU
RC
E: C
ERI,
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OD
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SOU
RC
E: C
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Page 21
SOU
RC
E: C
ERI,
Bak
er H
ugh
es.
SO
UR
CE:
CER
I, B
aker
Hu
ghe
s.
SOU
RC
E: C
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es.
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n-0
6J
an
-07
Ja
n-0
8J
an
-09
Ja
n-1
0J
an
-11
Ja
n-1
2J
an
-13
Ja
n-1
4
Oil-d
irec
ted
Gas-d
ire
cte
dG
as-d
ire
cte
d %
US
T
ota
l A
ctive
R
ig
s
0
500
1,0
00
1,5
00
2,0
00
2,5
00 Ja
n-0
6J
an
-07
Jan
-08
Jan
-09
Ja
n-1
0J
an
-11
Jan
-12
Ja
n-1
3J
an
-14
To
tal O
il-d
irec
ted
Go
M G
as-d
ire
cte
dO
nsh
ore
Gas-d
ire
cte
d
US
T
ota
l A
ctive
R
ig
s
0
20
40
60
80
100
12
0 Ja
n-0
6J
an
-07
Ja
n-0
8J
an
-09
Ja
n-1
0J
an
-11
Ja
n-1
2J
an
-13
Ja
n-1
4
Oil-d
irec
ted
Ga
s-d
ire
cte
d
US
G
ulf o
f M
ex
ic
o A
ctive
R
ig
s