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FIN5823FINANCIALMODELINGAPPLICATIONS1.pptx

FIN 5823 FINANCIAL MODELING ______________________________________________ Financial Modeling Applications

2

FINANCIAL MODELING APPLICATIONS

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For targeting purposes, the problem statement is: READ SLIDE

The strategy propose to solve this problem is:

First, READ SLIDE

Then, READ SLIDE

Finally, after the first two steps are completed, READ SLIDE

The advantage of this approach that it does not require any further division of the temperature intervals

And that heat pumping temperatures are treated as variables instead of fixed values

3

Scope of Discussion

We will discuss the definition and management of financial risk in

in any design process or decision making paradigm, like…

Extensions that are emerging are the treatment of other risks

in a multiobjective (?) framework, including for example

Investment Planning

Scheduling and more in general, operations planning

Supply Chain modeling, scheduling and control

Short term scheduling (including cash flow management)

Design of process systems

Product Design

Environmental Risks

Accident Risks (other than those than can be expressed

as financial risk)

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4

Introduction – Understanding Risk

Consider two investment plans, designs, or operational decisions

4

5

Conclusions

Risk can only be assessed after a plan has been selected but it cannot be

managed during the optimization stage (even when stochastic optimization

including uncertainty has been performed).

The decision maker has two simultaneous objectives:

There is a need to develop new models that allow not only assessing but managing

financial risk.

Maximize Expected Profit.

Minimize Risk Exposure

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6

What does Risk Management mean?

REDUCE THESE FREQUENCIES

OR…

INCREASE THESE FREQUENCIES

One wants to modify the profit distribution in order to satisfy the preferences of the decision maker

OR BOTH!!!!

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7

Characteristics of Two-Stage

Stochastic Optimization Models

Philosophy

Maximize the Expected Value of the objective over all possible realizations of

uncertain parameters.

Typically, the objective is Expected Profit , usually Net Present Value.

Sometimes the minimization of Cost is an alternative objective.

Uncertainty

Typically, the uncertain parameters are: market demands, availabilities,

prices, process yields, rate of interest, inflation, etc.

In Two-Stage Programming, uncertainty is modeled through a finite number

of independent Scenarios.

Scenarios are typically formed by random samples taken from the probability

distributions of the uncertain parameters.

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8

First-Stage Decisions

Taken before the uncertainty is revealed. They usually correspond to structural

decisions (not operational).

Also called “Here and Now” decisions.

Represented by “Design” Variables.

Examples:

Characteristics of Two-Stage

Stochastic Optimization Models

To build a plant or not. How much capacity should be added, etc.

To place an order now.

To sign contracts or buy options.

To pick a reactor volume, to pick a certain number of trays and size

the condenser and the reboiler of a column, etc

8

9

Second-Stage Decisions

Taken in order to adapt the plan or design to the uncertain parameters

realization.

Also called “Recourse” decisions.

Represented by “Control” Variables.

Example: the operating level; the production slate of a plant.

Sometimes first stage decisions can be treated as second stage decisions.

In such case the problem is called a multiple stage problem.

Shortcomings

The model is unable to perform risk management decisions.

Characteristics of Two-Stage

Stochastic Optimization Models

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10

Two-Stage Stochastic Formulation

LINEAR MODEL SP

s.t.

First-Stage Constraints

Second-Stage Constraints

Recourse

Function

First-Stage

Cost

First stage variables

Second Stage Variables

Technology matrix

Recourse matrix (Fixed Recourse)

Sometimes not fixed (Interest rates in Portfolio Optimization)

Complete recourse: the recourse cost (or profit) for every possible uncertainty realization remains finite, independently of the first-stage decisions (x).

Relatively complete recourse: the recourse cost (or profit) is feasible for the set of feasible first-stage decisions. This condition means that for every feasible first-stage decision, there is a way of adapting the plan to the realization of uncertain parameters.

We also have found that one can sacrifice efficiency for certain scenarios to improve risk management. We do not know how to call this yet.

Let us leave it linear because as is it is complex enough.!!!

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11

Robust Optimization Using Variance (Mulvey et al., 1995)

Previous Approaches to Risk Management

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

-2.5

-2.0

-1.5

-1.0

-0.5

0.0

0.5

1.0

1.5

2.0

2.5

3.0

3.5

4.0

4.5

5.0

5.5

Profit

Profit PDF

Expected

Profit

Variance is a measure

for the dispersion

of the distribution

Desirable Penalty

Maximize E[Profit] - ·V[Profit]

Underlying Assumption: Risk is monotonic with variability

Undesirable Penalty

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12

Robust Optimization Using Variance

Drawbacks

Variance is a symmetric risk measure: profits both above and below the target

level are penalized equally. We only want to penalize profits below the target.

Introduces non-linearities in the model, which results in serious computational

difficulties, specially in large-scale problems.

The model may render solutions that are stochastically dominated by others.

This is known in the literature as not showing Pareto-Optimality. In other words

there is a better solution (ys,x*) than the one obtained (ys*,x*).

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Robust Optimization using Upper Partial Mean (Ahmed and Sahinidis, 1998)

Previous Approaches to Risk Management

D(x)

0.0

0.1

0.2

0.3

0.4

-2.5

-2.0

-1.5

-1.0

-0.5

0.0

0.5

1.0

1.5

2.0

2.5

3.0

3.5

4.0

4.5

5.0

5.5

Profit

x

Profit PDF

UPM

= E[

D(x)

]

E[

x

]

UPM

= 0.50

UPM

= 0.44

Maximize E[Profit] - ·UPM

Underlying Assumption: Risk is monotonic with lower variability

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Robust Optimization using the UPM

Advantages

Linear measure

Robust Optimization using the UPM

Disadvantages

The UPM may misleadingly favor non-optimal second-stage decisions.

Consequently, financial risk is not managed properly and solutions with higher risk

than the one obtained using the traditional two-stage formulation may be obtained.

The model losses its scenario-decomposable structure and stochastic decomposition

methods can no longer be used to solve it.

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Robust Optimization using the UPM

 = 3 Profits s
Case I Case II Case I Case II
S1 150 100 0 0
S2 125 100 0 0
S3 75 75 25 6.25
S4 50 50 50 31.25
E[Profit] 100.00 81.25
UPM 18.75 9.38
Objective 43.75 53.13

Objective Function: Maximize E[Profit] - ·UPM

Downside scenarios are the same, but the UPM is affected by

the change in expected profit due to a different upside distribution.

As a result a wrong choice is made.

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Effect of Non-Optimal Second-Stage Decisions

Robust Optimization using the UPM

Both technologies are able to produce two products with different production cost and at different yield per unit of installed capacity

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OTHER APPROACHES

Cheng, Subrahmanian and Westerberg (2002, unpublished)

This paper proposes a new design paradigm of which risk is just one component.

We will revisit this issue later in the talk.

Multiobjective Approach: Considers Downside Risk, ENPV and Process

Life Cycle as alternative Objectives.

Multiperiod Decision process modeled as a Markov decision process

with recourse.

The problem is sometimes amenable to be reformulated as a sequence

of single-period sub-problems, each being a two-stage stochastic program

with recourse. These can often be solved backwards in time to obtain

Pareto Optimal solutions.

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OTHER APPROACHES

Risk Premium (Applequist, Pekny and Reklaitis, 2000)

Observation: Rate of return varies linearly with variability. The

of such dependance is called Risk Premium.

They suggest to benchmark new investments against the historical

risk premium by using a two objective (risk premium and profit)

problem.

The technique relies on using variance as a measure of variability.

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Conclusions

The minimization of Variance penalizes both sides of the mean.

The Robust Optimization Approach using Variance or UPM is not suitable

for risk management.

The Risk Premium Approach (Applequist et al.) has the same problems

as the penalization of variance.

THUS,

Risk should be properly defined and directly incorporated in the models to

manage it.

The multiobjective Markov decision process (Applequist et al, 2000)

is very closely related to ours and can be considered complementary. In

fact (Westerberg dixit) it can be extended to match ours in the definition

of risk and its multilevel parametrization.

Previous Approaches to Risk Management

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Financial Risk = Probability that a plan or design does not meet a certain profit target

Probabilistic Definition of Risk

zs is a new binary variable

Formal Definition of Financial Risk

Scenarios are independent events

For each scenario the profit is either

greater/equal or smaller than the target

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Financial Risk Interpretation

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Cumulative Risk Curve

Our intention is to modify the shape and location of this

curve according to the attitude towards risk of the decision maker

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Risk Preferences and Risk Curves

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Risk Curve Properties

A plan or design with Maximum E[Profit] (i.e. optimal in Model SP) sets a theoretical limit for financial risk: it is impossible to find a feasible plan/design having a risk curve entirely beneath this curve.

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Minimizing Risk: a Multi-Objective Problem

s.t.

.

.

.

Multiple Objectives:

At each profit we want minimize the associated risk

We also want to maximize the expected profit

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Restricted Risk MODEL

Risk Management

Constraints

s.t.

Forces Risk to be lower

than a specified level

Parametric Representations of the

Multi-Objective Model – Restricted Risk

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Parametric Representations of the

Multi-Objective Model – Penalty for Risk

s.t.

Penalty Term

Risk Penalty MODEL

Risk Management

Constraints

Define several profit

Targets and penalty

weights to solve the

model using a multi-

parametric approach

STRATEGY

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Advantages

Risk can be effectively managed according to the decision maker’s criteria.

The models can adapt to risk-averse or risk-taker decision makers, and their

risk preferences are easily matched using the risk curves.

A full spectrum of solutions is obtained. These solutions always have

optimal second-stage decisions.

Model Risk Penalty conserves all the properties of the standard two-stage

stochastic formulation.

Risk Management using the New Models

Disadvantages

The use of binary variables is required, which increases the computational

time to get a solution. This is a major limitation for large-scale problems.

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Computational Issues

Risk Management using the New Models

The most efficient methods to solve stochastic optimization problems reported

in the literature exploit the decomposable structure of the model.

This property means that each scenario defines an independent second-stage

problem that can be solved separately from the other scenarios once the first-

stage variables are fixed.

The Risk Penalty Model is decomposable whereas Model Restricted Risk is not.

Thus, the first one is model is preferable.

Even using decomposition methods, the presence of binary variables in both

models constitutes a major computational limitation to solve large-scale problems.

It would be more convenient to measure risk indirectly such that binary variables

in the second stage are avoided.

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Downside Risk (Eppen et al, 1989) =

Expected Value of the Positive

Profit Deviation from the target

Downside Risk

Positive Profit Deviation from

Target 

Formal definition of Downside Risk

The Positive Profit Deviation is

also defined for each scenario

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Downside Risk Interpretation

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Downside Risk & Probabilistic Risk

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Two-Stage Model using Downside Risk

s.t.

Penalty Term

MODEL DRisk

Downside

Risk Constraints

Advantages

Same as models using Risk

Does not require the use of

binary variables

Potential benefits from the

use of decomposition methods

Strategy

Solve the model using different

profit targets to get a full spectrum

of solutions. Use the risk curves to

select the solution that better suits

the decision maker’s preference

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34

Two-Stage Model using Downside Risk

Warning: The same risk may imply different Downside Risks.

Immediate Consequence:

Minimizing downside risk does not guarantee minimizing risk.

Click to edit Master text styles

Second level

Third level

Fourth level

Fifth level

34

35

Riskoptimizer (Palisades) and CrystalBall (Decisioneering)

Use excell models

Allow uncertainty in a form of distribution

Perform Montecarlo Simulations or use genetic algorithms

to optimize (Maximize ENPV, Minimize Variance, etc.)

Financial Software. Large variety

Some use the concept of downside risk

In most of these software, Risk is mentioned but not manipulated directly.

Commercial Software

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36

Process Planning Under Uncertainty

OBJECTIVES:

Maximize Expected Net Present Value

Minimize Financial Risk

Production Levels

DETERMINE:

Network Expansions

Timing

Sizing

Location

GIVEN:

Process Network

Set of Processes

Set of Chemicals

A

1

C

2

D

3

B

Forecasted Data

Demands & Availabilities

Costs & Prices

Capital Budget

36

37

Process Planning Under Uncertainty

Design Variables: to be decided before the uncertainty reveals

{

}

x

=

E

it

Y

it

,

,

Q

it

Y: Decision of building process i in period t

E: Capacity expansion of process i in period t

Q: Total capacity of process i in period t

Control Variables: selected after the uncertain parameters become known

S: Sales of product j in market l at time t and scenario s

P: Purchase of raw mat. j in market l at time t and scenario s

W: Operating level of of process i in period t and scenario s

{

}

ys

=

P

jlts

S

jlts

,

,

W

its

37

38

Example

Uncertain Parameters: Demands, Availabilities, Sales Price, Purchase Price

Total of 400 Scenarios

Project Staged in 3 Time Periods of 2, 2.5, 3.5 years

Process 1

Chemical 1

Process 2

Chemical 5

Chemical 2

Chemical 6

Process 3

Chemical 3

Process 5

Chemical 7

Chemical 8

Process 4

Chemical 4

38

39

Period 1

2 years

Period 2

2.5 years

Period 3

3.5 years

Process 1

Chemical 1

Chemical 5

Process 3

Chemical 3

Chemical 7

10.23 kton/yr

22.73 kton/yr

5.27 kton/yr

5.27 kton/yr

19.60 kton/yr

19.60 kton/yr

Process 1

Chemical 1

Chemical 5

Process 3

Chemical 3

Process 5

Chemical 7

Chemical 8

Process 4

Chemical 4

10.23 kton/yr

22.73 kton/yr

22.73 kton/yr

22.73 kton/yr

4.71 kton/yr

4.71 kton/yr

41.75 kton/yr

20.87 kton/yr

20.87 kton/yr

20.87 kton/yr

Chemical 1

Process 2

Chemical 5

Chemical 2

Chemical 6

Process 3

Chemical 3

Process 5

Chemical 7

Chemical 8

Process 4

Chemical 4

22.73 kton/yr

22.73 kton/yr

22.73 ton/yr

80.77 kton/yr

80.77 kton/yr

44.44 kton/yr

14.95 kton/yr

29.49 kton/yr

29.49 kton/yr

43.77 kton/yr

29.49 kton/yr

21.88 kton/yr

21.88 kton/yr

21.88 kton/yr

Process 1

Example – Solution with Max ENPV

39

40

Period 1

2 years

Period 2

2.5 years

Period 3

3.5 years

Process 1

Chemical 1

Chemical 5

Process 3

Chemical 3

Chemical 7

10.85 kton/yr

22.37 kton/yr

5.59 kton/yr

5.59 kton/yr

19.30 kton/yr

19.30 kton/yr

Process 1

Chemical 1

Chemical 5

Process 3

Chemical 3

Process 5

Chemical 7

Chemical 8

Process 4

Chemical 4

10.85 kton/yr

22.37 kton/yr

22.37 kton/yr

22.43 kton/yr

4.99 kton/yr

4.99 kton/yr

41.70 kton/yr

20.85 kton/yr

20.85 kton/yr

20.85 kton/yr

Process 1

Chemical 1

Process 2

Chemical 5

Chemical 2

Chemical 6

Process 3

Chemical 3

Process 5

Chemical 7

Chemical 8

Process 4

Chemical 4

22.37 kton/yr

22.37 kton/yr

22.77 ton/yr

10.85 kton/yr

10.85 kton/yr

7.54 kton/yr

2.39 kton/yr

5.15 kton/yr

5.15 kton/yr

43.54 kton/yr

5.15 kton/yr

21.77 kton/yr

21.77 kton/yr

21.77 kton/yr

Same final structure, different production capacities.

Example – Solution with Min DRisk(=900)

40

41

Example – Solution with Max ENPV

41

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Example – Risk Management Solutions

42

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Process Planning with Inventory

OBJECTIVES:

Maximize Expected Net Present Value

Minimize Financial Risk

The mass balance is modified such that now a certain level

of inventory for raw materials and products is allowed

A storage cost is included in the objective

PROBLEM DESCRIPTION:

A

1

2

D

3

B

D

MODEL:

43

44

Period 1

2 years

Period 2

2.5 years

Period 3

3.5 years

Chemical 5

Chemical 2

Chemical 6

51.95 kton/yr

22.36 kton/yr

Process 1

Process 2

5.14 kton/yr

12.48 kton/yr

1.05 kton/yr

16.28 kton/yr

Chemical 1

33.90

kton/yr

2.88 kton/yr

11.67 kton/yr

0.81 kton/yr

12.48 kton/yr

4.77 kton/yr

Chemical 6

Process 3

36.45 kton/yr

51.95 kton/yr

76.81 kton/yr

Process 1

1.62

kton

Chemical 5

10.28

kton

11.80 kton/yr

Chemical 2

2.11

kton

27.24 kton/yr

0.60 kton/yr

Chemical 7

4.65 kton/yr

31.09 kton/yr

Chemical 1

Chemical 3

39.04

kton/yr

35.74

kton/yr

5.75

kton

0.42 kton/yr

26.34 kton/yr

0.90 kton/yr

27.24 kton/yr

Process 2

1.18 kton/yr

Chemical 1

Chemical 6

Process 3

Chemical 3

Process 5

Chemical 8

Process 4

Chemical 4

26.77 kton/yr

36.45 kton/yr

26.77 kton/yr

76.81 kton/yr

76.81 kton/yr

43.14

kton/yr

25.41

kton/yr

Process 1

Process 2

3.86

kton

Chemical 7

11.64

kton

25.41 kton/yr

Chemical 5

7.32

kton

13.61 kton/yr

Chemical 2

3.86

kton

30.44 kton/yr

3.29 kton/yr

0.04 kton/yr

6.80

kton

1.94 kton/yr

11.91

kton

3.40 kton/yr

44.13 kton/yr

2.09 kton/yr

31.47 kton/yr

22.12 kton/yr

1.10 kton/yr

31.47 kton/yr

1.03 kton/yr

Example with Inventory – SP Solution

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45

Example with Inventory

Solution with Min DRisk (=900)

3.64 kton/yr

Process 3

22.15 kton/yr

11.23 kton/yr

Process 1

Chemical 5

5.80 kton/yr

Chemical 7

3.69 kton/yr

18.46 kton/yr

Chemical 1

Chemical 3

6.63

kton/yr

25.79

kton/yr

0.51 kton/yr

0.32 kton/yr

Chemical 1

Process 3

Chemical 3

Process 5

Chemical 8

Process 4

Chemical 4

23.38 kton/yr

22.15 kton/yr

23.38 kton/yr

11.23 kton/yr

5.73

kton/yr

1.64

kton/yr

Process 1

Chemical 7

7.38

kton

22.18 kton/yr

Chemical 5

0.64

kton

5.61 kton/yr

1.60 kton/yr

1.01

kton

0.02 kton/yr

7.27

kton

1.29 kton/yr

41.68 kton/yr

20.58 kton/yr

0.20 kton/yr

0.10 kton/yr

20.54 kton/yr

Chemical 1

Chemical 6

Process 3

Chemical 3

Process 5

Process 4

23.38 kton/yr

22.15 kton/yr

23.38 kton/yr

11.23 kton/yr

11.23 kton/yr

7.48

kton/yr

Process 1

Process 2

Chemical 7

3.37

kton

22.85 kton/yr

Chemical 5

0.90

kton

2.39 kton/yr

Chemical 2

5.39 kton/yr

0.96 kton/yr

1.07

kton

0.30 kton/yr

4.05

kton

1.16 kton/yr

43.72 kton/yr

0.26 kton/yr

5.39 kton/yr

22.04 kton/yr

5.39 kton/yr

Chemical 4

0.51

kton

Chemical 8

1.17

kton/yr

4.11

kton

23.00 kton/yr

0.15 kton/yr

Period 1

2 years

Period 2

2.5 years

Period 3

3.5 years

45

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Example with Inventory - Solutions

With Inventory

Without

Inventory

DRisk

DRisk

46

47

Downside Expected Profit

Definition:

Up to 50% of risk (confidence?) the lower ENPV solution has higher profit expectations.

47

48

Value at Risk

Definition:

VaR=zp for symmetric distributions (Portfolio optimization)

VaR is given by the difference between the mean value of the profit and the profit value corresponding to the p-quantile.

48

49

COMPUTATIONAL APPROACHES

Sampling Average Approximation Method:

Solve M times the problem using only N scenarios.

If multiple solutions are obtained, use the first stage variables to solve the

problem with a large number of scenarios N’>>N to determine the optimum.

First Stage variables are complicating variables.

This leaves a primal over second stage variables, which is decomposable.

Generalized Benders Decomposition Algorithm

49

50

2005 2030

Example

Generate a model to:

Evaluate a large network of natural gas supplier-to-market transportation alternatives

Identify the most profitable alternative(s)

Manage financial risk

51

Australia

Indonesia

Iran

Kazakhstan

Malaysia

Qatar

Russia

Network of Alternatives

Suppliers

China

India

Japan

S. Korea

Thailand

United States

Markets

Transportation Methods

LNG

CNG

Ammonia

Methanol

Pipeline

GTL

52

Network of Alternatives

53

Results

Risk Management (Downside Risk):

Malaysia

GTL

Thailand

China

54

Value at Risk (VaR):

VaR is the expected loss for a certain confidence level usually set at 5%

VaR =ENPV – NPV @ p-quantile

Opportunity Value (OV) or Upper Potential (UP):

OV = NPV @ (1-p)-quantile – ENPV

55

Results

Value at Risk (VaR) and Opportunity Value (OV):

Reduction in VaR: 18.1% Reduction in OV: 18.9%

56

Results

Risk /Upside Potential Loss Ratio

Risk /Upside Potential Loss Ratio: 2.2

57

Risk /Upside Potential Loss Ratio

Risk /Upside Potential Loss Ratio

where:

58

Upper and Lower Bound Risk Curve

The curve constructed by plotting the set of net present values (NPV) for the best design under each scenario.

Upper Bound Risk Curve (Envelope):

59

Upper and Lower Bound Risk Curve

The curve constructed by plotting the set of net present values (NPV) for the worst (of the set of best designs) under each scenario.

Lower Bound Risk Curve:

60

Results

Upper and Lower Bound Risk Curve

61

Conclusions

A probabilistic definition of Financial Risk has been introduced in the framework of two-stage stochastic programming. Theoretical properties of

related to this definition were explored.

Using downside risk leads to a model that is decomposable in scenarios and that

allows the use of efficient solution algorithms. For this reason, it is suggested

that this model be used to manage financial risk.

New formulations capable of managing financial risk have been introduced.

The multi-objective nature of the models allows the decision maker to choose

solutions according to his risk policy. The cumulative risk curve is used as a

tool for this purpose.

To overcome the mentioned computational difficulties, the concept of Downside

Risk was examined, finding that there is a close relationship between this

measure and the probabilistic definition of risk.

The models using the risk definition explicitly require second-stage binary variables. This is a major limitation from a computational standpoint.

An example illustrated the performance of the models, showing how the risk

curves can be changed in relation to the solution with maximum expected profit.

61

Profit Histogram

0.00

0.05

0.10

0.15

0.20

0.25

0.30

0.35

0.40

0.45

-300-200-1000100200300400500600700800

Profit (M$)

Probability

Investment Plan I - E[Profit] = 338

Investment Plan II - E[Profit] = 335

Probability of Loss

for Plan I = 12%

0.00

0.02

0.04

0.06

0.08

0.10

0.12

0.14

0.16

0.18

0.20

-300-200-1000100200300400500600700800

Profit

x

Probability

xcyqpMax

T

s

s

T

ss

bAx

Xxx 0

sss

hWyxT 

0

s

y



s

Sk

kks

ProfitProfitpMax ; 0



Ss

ss

pUPM

-380

-360

-340

-320

-300

-280

-260

-240

-220

-200

01234567891011121314151617

UPM

E[Profit]

Robustness Solution

Robustness Solution with

Optimal Second-Stage Decisions

P1

A

P2B

P1

A

P2B

P1

A

P2B

-380

-360

-340

-320

-300

-280

-260

-240

-220

-200

020406080100120140160180200220

r

E[Profit]

Robustness Solution

Robustness Solution with

Optimal Second-Stage Decisions

0

2

4

6

8

10

12

14

16

18

020406080100120140160180200220

r

UPM

Robustness Solution

Robustness Solution with

Optimal Second-Stage Decisions

 

 ProfitPxRisk ),(

 



s

ss

ProfitPpxRisk ),(

 





else0

If1

s

s

Profit

ProfitP

 

ss

zProfitP 



s

ss

zpxRisk ),(

0.00

0.02

0.04

0.06

0.08

0.10

0.12

0.14

0.16

0.18

0.20

Profit

x

Probability

Cumulative Probability = Risk(x,

W

)

W

0.00

0.02

0.04

0.06

0.08

0.10

0.12

0.14

Profit

x

Area = Risk(x,

W

)

W

x fixed

Profit PDF f

(x)

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

2505007501000125015001750200022502500275030003250

Profit (M$)

Risk

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

-2.0-1.5-1.0-0.50.00.51.01.52.02.53.03.54.0

Profit

Risk

Risk-Averse

Investor's Choice

E[Profit] = 0.4

Risk-Taker

Investor's Choice

E[Profit] = 1.0

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

Profit

Risk

Maximum

E[Profit]

Impossible

curve

Possible

curve

)1,0(

)1(





s

ss

T

s

T

s

ss

T

s

T

s

z

zUxcyq

zUxcyq

Xxx 0

0

s

y



xcyqp ProfitMax E

T

s

sss







s

ss

zp Min Risk

11





s

sisi

zp Min Risk

bAx

sss

hWyxT 

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

Target Profit

W

Risk

x fixed

W

1

W

2

W

3

W

4

Min Risk(x,

W

1

)

Min Risk(x,

W

2

)

Min Risk(x,

W

3

)

Min Risk(x,

W

4

)

Max E[Profit(x)]

xcyqpMax

T

s

sss

i

s

sis

εzp

)1,0(

)1(





s

sisi

T

s

T

s

sisi

T

s

T

s

z

zUxcyq

zUxcyq

Xxx 0

0

s

y

bAx

sss

hWyxT 





is

sisi

T

s

s

T

ss

zpxc yqpMax

)1,0(

)1(





s

sisi

T

s

T

s

sisi

T

s

T

s

z

zUxcyq

zUxcyq

Xxx 0

0

s

y

bAx

sss

hWyxT 



 

 ,, xExDRisk



 





Otherwise0

If

,

xProfitxProfit

x





s

ss

pxDRisk ,





Otherwise0

If

ss

s

ProfitProfit

0.00

0.02

0.04

0.06

0.08

0.10

0.12

0.14

Profit

x

W

x fixed

DRisk(x,

W

) = E[

d

(x,

W

)]

Profit PDF f

(x)

()

ò

W

¥-

xxx-W=W dfxDRisk )(),(

d

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

Profit

x

Risk

(

x

,

x

)

x

fixed

W

Area =

DRisk

(

x

,

W

)

ò

W

¥

-

x

x

=

W

d

x

Risk

x

DRisk

)

,

(

)

,

(







s

ss

T

s

s

T

ss

pxc yqpMax

)( xcyq

T

s

T

ss



Xxx 0

0

s

y

bAx

sss

hWyxT 

0

s

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

-2.0-1.5-1.0-0.50.00.51.01.52.02.53.03.54.0

Profit

Risk

DRisk(Design I , 0.5) = 0.2

Risk(Design I , 0.5) = 0.5

DRisk(Design II , 0.5) = 0.2

Risk(Design II , 0.5) = 0.309

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

2505007501000125015001750200022502500275030003250

NPV (M$)

Risk

PP solution

E[NPV] = 1140 M$

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

2505007501000125015001750200022502500275030003250

NPV (M$)

Risk

PP

500

600

700

800

900

1000

1100

1200

1300

1400

1500

W

increases

W

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

2505007501000125015001750200022502500275030003250

NPV (M$)

Risk

W

= 900

ENPV = 908

W

= 1100

ENPV = 1074

PP

ENPV =1140

0.0000

0.0002

0.0004

0.0006

0.0008

0.0010

0.0012

0.0014

0.0016

0.0018

0.0020

0.0022

0.0024

0.0026

050010001500200025003000

NPV

(

x

, M$ )

NPV PDF f(x)

W

= 900

W

= 1100

PP

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

02505007501000125015001750200022502500275030003250350037504000

NPV (M$)

Risk

PP solution

E[NPV] = 1140 M$

PPI solution

E[NPV] = 1237 M$

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

02505007501000125015001750200022502500275030003250350037504000

NPV (M$)

Risk

W

= 900

ENPV = 980

W

= 1400

ENPV = 1184

PPI

ENPV = 1140

PPI

ENPV = 1237

)

,

(

)

,

(

)

,

(

)

,

(

W

-

W

W

=

=

ò

W

¥

-

W

x

DRisk

x

Risk

d

x

f

p

x

DENPV

x

x

x

0

125

250

375

500

625

750

875

1000

1125

1250

0.00.10.20.30.40.50.60.70.80.91.0

Risk

CEP (M$)

PP solution

E[NPV] = 1140 M$

W = 900

E[NPV] = 908 M$

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

2505007501000125015001750200022502500275030003250

NPV (M$)

Risk

W

= 900

W

= 1100

PP

)

,

(

)]

(

[

)

,

(

1

W

-

=

-

W

x

Risk

x

Profit

E

p

x

VaR

)]

(

[

x

Profit

E

)

,

(

W

p

x

VaR

0.00

0.02

0.04

0.06

0.08

0.10

0.12

0.14

Profit

x

Area = Risk(x,

W

)

W

x fixed

Profit PDF

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

0

1

2

3

4

5

6

7

8

9

10

1s

4.666

DR-200s

4.640

200s

4.678

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

012345678910

Indo-GTL

Ships: 5 & 3

ENPV:4.633

DR@ 4: 0.190

DR@ 3.5: 0.086

Mala-GTL

Ships: 4 & 2

ENPV:4.570

DR@ 4: 0.157

DR@ 3.5: 0.058

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

012345678910

Indo-GTL

Ships: 5 & 3

ENPV:4.633

DR@ 4: 0.190

DR@ 3.5: 0.086

Mala-GTL

Ships: 4 & 2

ENPV:4.570

DR@ 4: 0.157

DR@ 3.5: 0.058

VaR @ 5%: 1.49

VaR @ 5%: 1.82

OV @ 95%: 1.75

OV @ 95%: 1.42

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

0

1

2

3

4

5

6

7

8

9

10

Indo-GTL

Ships: 5 & 3

ENPV:4.633

DR@ 4: 0.190

DR@ 3.5: 0.086

Mala-GTL

Ships: 4 & 2

ENPV:4.570

DR@ 4: 0.157

DR@ 3.5: 0.058

VaR @ 5%: 1.49

VaR @ 5%: 1.82

OV @ 95%: 1.75

OV @ 95%: 1.42

O-Area: 0.116

R-Area: 0.053

ò

ò

¥

+

¥

-

+

¥

-

-

=

=

dNPV

dNPV

R_Area

O_Area

y

y

þ

ý

ü

î

í

ì

³

=

+

otherwise

if

0

0

y

y

y

þ

ý

ü

î

í

ì

<

-

=

-

otherwise

if

0

0

y

y

y

)

(

)

(

NPV

Risk

NPV

Risk

DR

NGC

NGC

-

-

=

y

0.0

0.1

0.2

0.3

0.4

0.5

0.6

0.7

0.8

0.9

1.0

012345678910

NPV

Risk

O_Area

R_Area

Risk(x

1

,NPV)

Risk(x

2

,NPV)

ENPV

1

ENPV

2

0

0.2

0.4

0.6

0.8

1

0.00

2.00

4.00

6.00

8.00

10.00

Risk

a) Possible

b) Possible

E) Envelope

0

0.2

0.4

0.6

0.8

1

0.0

2.0

4.0

6.0

8.0

10.0

Risk

d) Impossible

c) Impossible

E) Envelope

s

\

d

s

1

s

2

s

3

s

n

d

1

NPV

d1,s1

NPV

d2,s1

NPV

d3,s1

NPV

dn,s1

d

2

NPV

d1,s2

NPV

d2,s2

NPV

d3,s2

NPV

dn,s2

d

3

NPV

d1,s3

NPV

d2,s3

NPV

d3,s3

NPV

dn,s3

:

:

:

:

:

:

:

:

:

:

d

n

NPV

d1,sn

NPV

d2,sn

NPV

d3,sn

NPV

dn,sn

Min

Min

s1

NPV

Min

s2

NPV

Min

s3

NPV

Min

sn

NPV

0.0

0.2

0.4

0.6

0.8

1.0

0.01.02.03.04.05.06.07.08.09.0

Indo-GTL

Ships: 6 & 3

ENPV:4.63

Mala-GTL

Ships: 4 & 3

ENPV:4.540

Upper Envelope

ENPV:4.921

Lower Envelope

ENPV:3.654