IH2 Technology: Commercial Progress and Product Quality Update

DisclaimerThis presentation contains forward-looking statements concerning the financial condition, results of operations and businesses of Royal Dutch Shell. All statements other than statements of historical fact are, or may be deemed to be, forward-looking statements. Forward-looking statements are statements of future expectations that are based on management’s current expectations and assumptions andinvolve known and unknown risks and uncertainties that could cause actual results, performance or events to differ materially from those expressed or implied in these statements. Forward-looking statements include, among other things, statements concerning the potential exposure of Royal Dutch Shell to market risks and statements expressing management’s expectations, beliefs, estimates, forecasts, projections and assumptions. These forward-looking statements are identified by their use of terms and phrases such as ‘‘anticipate’’, ‘‘believe’’, ‘‘could’’, ‘‘estimate’’, ‘‘expect’’, ‘‘goals’’, ‘‘intend’’, ‘‘may’’, ‘‘objectives’’, ‘‘outlook’’, ‘‘plan’’, ‘‘probably’’, ‘‘project’’, ‘‘risks’’, ‘‘seek’’, ‘‘should’’, ‘‘target’’, ‘‘will’’ and similar terms and phrases. There are a number of factors that could affect the future operations of Royal Dutch Shell and could cause those results to differ materially from those expressed in the forward-looking statements included in this presentation, including (without limitation): (a) price fluctuations in crude oil and natural gas; (b) changes in demand for Shell’s products; (c) currency fluctuations; (d) drilling and production results; (e) reserves estimates; (f) loss of market share and industry competition; (g) environmental and physical risks; (h) risks associated with the identification of suitable potential acquisition properties and targets, and successful negotiation and completion of such transactions; (i) the risk of doing business in developing countries and countries subject to international sanctions; (j) legislative, fiscal and regulatory developments including regulatory measures addressing climate change; (k) economic and financial market conditions in various countries and regions; (l) political risks, including the risks of expropriation and renegotiation of the terms of contracts with governmental entities, delays or advancements in the approval of projects and delays in the reimbursement for shared costs; and (m) changes in trading conditions. All forward-looking statements contained in this presentation are expressly qualified in their entirety by the cautionary statements contained or referred to in this section. Readers should not place undue reliance on forward-looking statements. Additional factors that may affect future results are contained in Royal Dutch Shell’s 20-F for the year ended December 31, 2013 (available at www.shell.com/investor and www.sec.gov ). These factors also should be considered by the reader. Each forward-looking statement speaks only as of the date of this presentation, 17 June 2014

Neither Royal Dutch Shell nor any of its subsidiaries undertake any obligation to publicly update or revise any forward-looking statement as a result of new information, future events or other information. In light of these risks, results could differ materially from those stated, implied or inferred from the forward-looking statements contained in this presentation.

Main Points

• Why IH2 technology?

• Integration with existing assets

• Commercialization Process

• Product Quality Update

• Executive Summary

Why IH2 Technology?• Self-sufficient, self-contained and self-sustaining

• Feedstock flexible, product yields 67-172 gal/ton (MAF) Spans gasoline, jet and diesel range

No detectable oxygen or TAN

• High GHG reductions

• Integrates commercially proven equipment; Market Ready

• Attractive economics (standalone or co-locate with existing assets)

• Improved catalysts enhanced product yield & quality

• Available exclusively from CRI Catalyst Company

Why IH2 Technology?

Distilled Hydrocarbon

Hi Pressure Steam

Clean Water

Fertilizer

BioChar

Biogenic CO2

Crop Residue

City Waste

Wood/ForestResidue

Energy Crops

Algae

Feed

Products

2) Fluidized Bed

Proprietary Catalyst System

Renewable H2

340-470C<500psig

1) Feed ConditioningSizing , Drying & Feeding

1st Stage 2nd Stage

3) Fixed Bed

Proprietary Catalyst SystemRenewable H2

<500psig

4) SMR C1-C3 GasRenewable H2

Process

5) Cyclones

Gasoline, Jet and DieselHydrocarbons (67-172 gal/ton)R100 Regular Gasoline (Wood)R100 Intermediate Gasoline (Wood) R100 Diesel (Wood)

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Option 1: Full StandaloneLocation Flexibility, Minimum Environmental ImpactMaximum GHG reductionLowest CI productHighest Capital CostNo Fixed Cost Synergy

Option 2: Integrated with Refinery HTMinimum Environmental ImpactLowest CI productMaximum GHG reductionLower Capital CostSome Fixed Cost Synergy

Option 3 Integrated with Refinery H2

Higher Environmental ImpactReduced GHG reductionHigher CI productLowest Capital CostCapital ~25% lower than base case

Integration - Refinery

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IH2 UnitBagasse

Cane Trash/Sugar Cane Tops

SugarCane

Sugar Factory

EnhancedEnergy

Integration

Hot water

HP SteamCo-Gen

Sale to grid

SugarMolasses

Fuels

Boiler

Char

LP Steam

Integration – Sugar Mill

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Growth Harvest Extraction

Primary Product(s)

Residues

NH3 / S / Ash

LP Steam / Hot Water

CO2

HP Steam or HP Steam to Power

Fuel

100 gal/ton MAF70% gasoline/ 30%

diesel

Integration – Algae Facility

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Growth Harvest ExtractionWhole Algae

NH3 / S / Ash

LP Steam / Hot Water

CO2

HP Steam or HP Steam to Power

Fuel

157 -172 gal/ton MAF(50% gasoline/

50% diesel)

Integration – Algae Facility

• Wood Supply System– Procurement staff & buyer networks/intellectual capital

– Fiber Supply Agreements

– Landowner data: US RFS-2 “chain-of-custody” requirements

• Contract data – ownership & legal description

• Load tickets – link delivered loads to harvest location

• Harvest location maps – spatial data

• Fiber Accounting & Information Systems Integration

• HSE Systems – Air & water permits

– Sampling & reporting structure/agency interaction

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10

Integration – Paper Mill, “Soft Assets”

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11

Integration – Paper Mill, “Hard Assets”

Paper ProcessDigestion, refining,

washing, paper machines Paper

Hea

t

LP Steam / Heat

Power

Fuel

90 gal/ton MAF65% gasoline/ 35%

diesel

Char Boiler/Co-Gen

Wood YardHandling, storage,chipping, drying, hammer milling

LP S

team

or

Pow

er

to grid

Biomass Feedstock

Chips

Ch

ar

Multiple uses for low-grade heat or power

Soft Assets

LP S

team

/ P

ow

er

0.02L/dayBangalore 1L/week

Chicago, Bangalore

22L/dayChicago

2000L/day

NanoScale EE HT toolsGTI/CRI Design BasisCommercially EngineeredCommercially Fabricated

1st Stage System2nd Stage SystemOn line analytical suite

Up to 16 runs/day/system

Chicago Unit GTI Design BasisGTI Built

Bangalore Unit GTI/CRI Design BasisCommercially EngineeredCommercially FabricatedMixture online/offline

Up to 3 runs/week

GTI Design BasisCommercially EngineeredCommercially Fabricated

Mixture Online/Offline

Up to 1 run/week

GTI/CRI Design BasisCommercially Engineered

Mixture Online/Offline

Up to 3 runs/month

Commercialization Process

Commercialization Process – 3D Render

Product Quality – MBU Scale

Hydrocarbon

Water

Total Liquid Product 2nd Gen Catalysts Lab Scale

Total Liquid Product 1st Gen Catalysts Lab Scale

Hydrocarbon

Water

Gas/Jet/Diesel Product 3rd Gen Catalysts Lab Scale

4Q09 “R5” 3Q10 “R25” 2Q12 “R60+”

Improve product yield, appearance and quality

Jet/Diesel Product 4th Gen Catalysts Lab Scale

1Q14 “R100”

Product Quality – Pilot Scale

Gasoline Product 3rd Gen Catalyst Drop In / Tank ReadyUS R100 Quality (RBOB)

Jet/Diesel Product 3rd Gen Catalyst US R100 Diesel

Water Product 3rd Gen Catalyst Clean, No CarbonContains NH3/H2S (lacks commercial design water clean up )

US

• Gasoline (from wood): R100 Meets ASTM D-4814-10b

~86 Octane

S < 15-ppm

Fully renewable premium RBOB

• Diesel (from wood) R100 Meets ASTM D-975-11

Cetane Number 44

S < 10-ppm

Product Quality SummaryEurope:

• Petrol (from wood) Petrol (from wood)

EN 228: Petrol – Jan 2009

Octane Low

S ~10-ppm

• Diesel (from wood) EN 590:2009+A1:2010

Cetane # Low

S ~15-ppm

• 3rd Party Testing Underway in 2H2014

• More Upgrading Wood Product for EU Specs

Executive Summary• Self-sufficient, self-contained and self-sustaining

• Feedstock flexible, product yields 67-172 gal/ton (MAF) Spans gasoline, jet and diesel range

No detectable oxygen or TAN

• High GHG reductions

• Integrates commercially proven equipment; Market Ready

• Attractive economics (standalone or co-locate with existing assets)

• Improved catalysts enhanced product yield & quality

• Available exclusively from CRI Catalyst Company

Thank You

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Learn more at http://www.cricatalyst.com/catalysts/renewables.html