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0000950134-07-014793.txt : 200707060000950134-07-014793.hdr.sgml : 2007070620070706164036ACCESSION NUMBER:0000950134-07-014793CONFORMED SUBMISSION TYPE:8-KPUBLIC DOCUMENT COUNT:38CONFORMED PERIOD OF REPORT:20070706ITEM INFORMATION:Regulation FD DisclosureITEM INFORMATION:Financial Statements and ExhibitsFILED AS OF DATE:20070706DATE AS OF CHANGE:20070706

FILER:

COMPANY DATA:COMPANY CONFORMED NAME:VALERO ENERGY CORP/TXCENTRAL INDEX KEY:0001035002STANDARD INDUSTRIAL CLASSIFICATION:PETROLEUM REFINING [2911]IRS NUMBER:741828067STATE OF INCORPORATION:DEFISCAL YEAR END:1231

FILING VALUES:FORM TYPE:8-KSEC ACT:1934 ActSEC FILE NUMBER:001-13175FILM NUMBER:07967774

BUSINESS ADDRESS:STREET 1:P.O. BOX 696000CITY:SAN ANTONIOSTATE:TXZIP:78269-6000BUSINESS PHONE:2103452000

MAIL ADDRESS:STREET 1:P.O. BOX 696000CITY:SAN ANTONIOSTATE:TXZIP:78269-6000

8-K1d48053e8vk.htmFORM 8-K

e8vk

Table of Contents

UNITED STATES
SECURITIES AND EXCHANGE COMMISSION

Washington, D.C. 20549

FORM 8-K

CURRENT REPORT

Pursuant to Section13 or 15(d) of theSecurities Exchange Act of 1934

Dateof Report (Date of earliest event reported): July6, 2007

VALERO ENERGY CORPORATION

(Exact name of registrant as specified in its charter)

Delaware
(State or other jurisdiction
of incorporation)

1-13175
(Commission File Number)

74-1828067
(IRS Employer
Identification No.)

One Valero Way
San Antonio, Texas
(Address of principal executive offices)

78249
(Zip Code)

Registrants telephone number, including area code: (210) 345-2000

Check the appropriate box below if the Form 8-K filing is intended to simultaneously satisfythe filing obligation of the registrant under any of the following provisions (see GeneralInstruction A.2. below):

o Written communications pursuant to Rule425 under the Securities Act (17 CFR 230.425)

o Soliciting material pursuant to Rule14a-12 under the Exchange Act (17 CFR 240.14a-12)

o Pre-commencement communications pursuant to Rule14d-2(b) under the Exchange Act (17 CFR240.14d-2(b))

o Pre-commencement communications pursuant to Rule13e-4(c) under the Exchange Act (17 CFR240.13e-4(c))

TABLE OF CONTENTS

Item7.01 RegulationFD DisclosureItem9.01 Financial Statements and ExhibitsSIGNATUREEXHIBIT INDEXSlides From Presentation

Table of Contents

Item7.01 Regulation FD Disclosure.

Senior management of Valero Energy Corporation (the Company) will be meeting with investors onJuly9, 2007, at which time the slides attached to this report will be presented. The slides areincluded in Exhibit99.1 to this report and are incorporated herein by reference. The slides willbe available on the Companys website at www.valero.com.

The information in this report is being furnished, not filed, pursuant to RegulationFD.Accordingly, the information in Items 7.01 and 9.01 of this report will not be incorporated byreference into any registration statement filed by the Company under the Securities Act of 1933, asamended, unless specifically identified therein as being incorporated therein by reference. Thefurnishing of the information in this report is not intended to, and does not, constitute adetermination or admission by the Company that the information in this report is material orcomplete, or that investors should consider this information before making an investment decisionwith respect to any security of the Company or any of its affiliates.

Safe Harbor Statement

Statements contained in the exhibit to this report that state the Companys or its managementsexpectations or predictions of the future are forward-looking statements intended to be covered bythe safe harbor provisions of the Securities Act of 1933 and the Securities Exchange Act of 1934.It is important to note that the Companys actual results could differ materially from thoseprojected in such forward-looking statements. Factors that could affect those results includethose mentioned in the documents that the Company has filed with the Securities and ExchangeCommission.

Item9.01 Financial Statements and Exhibits.

(d)Exhibits.

99.1 Slides from presentation to be used on July9, 2007.

2

Table of Contents

SIGNATURE

Pursuant to the requirements of the Securities Exchange Act of 1934, the Company has duly causedthis report to be signed on its behalf by the undersigned hereunto duly authorized.

VALERO ENERGY CORPORATION

Date: July 6, 2007 By: /s/ Jay D. Browning

Jay D. Browning

Senior Vice President and Secretary

3

Table of Contents

EXHIBIT INDEX

Number Exhibit

99.1

Slides from presentation to be used on July9, 2007.

4

EX-99.12d48053exv99w1.htmSLIDES FROM PRESENTATION

exv99w1

Exhibit99.1

Basics of RefiningDesulfurizationHydrocrackingValero Refining SystemBenicia Refinery OperationsCARB Gasoline with 10% EthanolPlant Tour

Rich MarcoglieseExecutive Vice President Refining Operations

Crudes are classified and priced by density and sulfur content Crude density is commonly measured by API gravityAPI gravity provides a relative measure of crude oil densityThe higher the API number, the lighter the crudeLight crudes are easier to processHeavy crudes are more difficult to processCrude sulfur content is measured as a percentageLess than 0.7% sulfur content = sweetGreater than 0.7% sulfur content = sourHigh sulfur crudes require additional processing to meet regulatory specsAcid content is measured by Total Acid Number (TAN)Acidic crudes highly corrosive to refinery equipmentHigh acid crudes are those with TAN greater than 0.7

Source: Industry reportsNOTE: Red line represents the average crude quality by decade (actual and projected)Majority of global reserves are light/medium sour Most quoted benchmark prices are light sweet crudesWTI (West Texas Intermediate), Western HemisphereBrent (North Sea Crude), EuropeHistorical trend shows global crude supply becoming heavier and more sour

Crude TypesCharacteristicsYields2005 U.S.3%34 API GravityProductionLight Sweet Crude30%0.7 % Sulfur(e.g. WTI, Brent, Saharan Refinery34%7%Blend)35% DemandGases Most Expensive33%Gasoline RFG50% Conventional3%CARB24 34 API GravityMedium Sour Crude21%Premium 0.7 % Sulfur(e.g. Mars, Arab Light,26% Arab Medium, Urals)50% Demand33% Distillate50%Less ExpensiveJet Fuel Diesel Heating Oil24 API Gravity 1%14%Heavy 0.7 % Sulfur22%10%Fuel Oil &Heavy Sour CrudeOther(e.g. Maya, Cerro Negro, Cold 15% DemandLake, Western Canadian Select)63%Source: EIA Refiner ProductionLeast Expensive

Refineries upgrade crude oil to higher value products

IntermediatesFinal Products90FPropane, Butane Refinery fuel gas and lighter Propane NGLs 90-220FStraight Run MoreGasoline (low Gasoline (high octane) octane)processingCrude oil220-315FMore Gasoline (high octane) Naphtha Distillationprocessing Jet fuel Tower (Crude Kerosene Unit)315-450FMore Jet fuel Kerosene processing DieselFuel oilMore Gasoline (high octane) 450-650FLight Gas Oil Furnace Diesel processingFuel oilMore Gasoline (high octane) 650-800FHeavy Gas Oil Diesel Vacuumprocessing Fuel oil Unit Gasoline (high octane) 800+FResidual Fuel More Diesel Oil/Asphalt Fuel oil processingLube stocks

Crude UnitPropane/Butane4% Propane/ ButaneGasolineLow Octane Gasoline Reformer High Octane GasolineRFGTowerand Naphtha30% Conventional CARBHydrogenPremiumLightDistillationHS Kerosene/Jet FuelDistillateLS Kerosene/Jet FuelSweetDesulfurizer34% DistillateCrudeJet Fuel DieselHS Diesel/Heating OilLS Diesel/Heating OilHeating OilVacuum Gas OilHeavy32% Fuel Oil & UnitOtherHeavy Fuel Oil100% Total YieldSimple, low upgrading capability refineries run sweet crude

Crude Atmospheric TowerVacuum TowerReformer

CrudeUnitPropane/Propane/Butane8%Butane GasolineReformerRFGLow Octane Gasoline High Octane Gasoline45% Conventional and NaphthaCARBTowerPremiumHydrogenDistillateLightDistillationHS Kerosene/Jet FuelLS Kerosene/Jet FuelDesulfurizer27% DistillateSourJet FuelHS Diesel/Heating OilLS Diesel/Heating OilDieselCrudeHeating OilLight Cycle Oil(LCO)AlkylationUnitAlkylateFluid CatalyticVacuum Gas OilCrackerUnit(FCC)FCC GasolineHeavy 24% Fuel Oil & OtherHeavy Fuel Oil104% Total YieldModerate upgrading capability refineries tend to run more sour crudes while achieving increased higher value product yields and volume gain

Crude Hydrogen PlantGasUnitPropane/Propane/Butane7%Butane Gasoline RFGTowerLow Octane Gasoline ReformerHigh Octane Gasoline58% Conventional and NaphthaCARBPremiumMedium/DistillationHydrogenHeavyDistillate28% DistillateHS Kerosene/Jet FuelLS Kerosene/Jet FuelSour DesulfurizerJet Fuel DieselCrudeHS Diesel/Heating OilLS Diesel/Heating OilHeating OilHydrocrackerHydrocrackate Gasoline Light Gas Oil Ultra Low Sulfur Jet/Diesel LCOAlkylationUnitAlky GasolineFluid CatalyticMedium Gas Oil Cracker (FCC)VacuumFCC GasolineUnitHeavy 15% Fuel Oil & DelayedOtherHeavy Fuel OilCokeCoker108% Total YieldComplex refineries can run heavier and more sour crudes while achieving the highest light product yields and volume gain

Fluidized Catalytic Cracker

Hydrocracker Reactors

Delayed CokerSuperstructure holds the drill and drill stemFluid Coker Benicia while the coke is forming in the drum

Need conversion capacity to capitalize on sour crude discountsHydroskim Breakeven or moderate margins; High resid yieldWhen margins are positive increase crude runsWhen margins are negative decrease crude runsCracking Better margins; Lower resid yieldCoking Best margins; Lowest resid yieldMaximize heavy crudes

ObjectiveRemove sulfur from light products (gasoline or diesel) to meet air quality requirements for clean burning fuels

ObjectiveValue added upgrading of high sulfur distillates to low sulfur gasoline and ultra low sulfur jet/diesel to meet air quality requirements for clean burning fuels

Throughput capacities in thousand barrels per day; Excludes 165,000 bpd Lima, Source: Company reports; VLO figures exclude Lima, OH refinery OH refinery3.1million barrels per day of High-complexity system and throughput capacityleader in conversion capacityScale helps mitigate effect of specific Enables us to convert more low-outagesquality, discounted feedstocks intoGeographically diverse high-quality productsValero participates in four key regions Refining system designed for feedstock flexibility Optimization among regional refining systems Increased variety of heavy sour and resid feedstocks from 27 in 2002 to 40 in 2006

Continued commitment to OSHAs Voluntary Protection Program (VPP)VPP is a recognized OSHA program for excellence in safetyValero has 11 of only 23 VPP Star Sites in the U.S.New Process SafetyManagement (PSM)initiative underwayCreated VP position in Operations to focus efforts on safetyAchieve best-in-class PSM at all our facilities

Doug ComeauVice President and General Manager Benicia Refinery

Built by Exxon in 1969 on the site of the former Benicia Army Arsenal Significant modifications and upgrades have made the refinery one of the most complex and profitable refineries in the United States Valero acquired the refinery in 2000 and has made additional improvements since that time Valero acquired Huntway Refining Company in 2001

Recognized as an OSHA VPP Star Site September2006 Total throughput of 170,000 bpd Primary products include CARBOB gasoline, diesel, jet fuel, LPG, fuel oil and asphalt High conversion operation 70%+ gasoline yield Located on 425 acres with 475 acre buffer zone Staffed by 480 full-time employees 200 continuing service contractors

Crude slate includes Alaska North Slope (ANS), San Joaquin Valley (SJV)and a wide variety of other crudes80% received by ship across Refinery docks20% received by pipelineShifting crude slateWhen acquired in 2000, 80% of Benicias crude was ANSToday, less than 40% ANSVersatile, high-conversion facility with ability to process heavy, sour crudes35% heavy sour, 47% medium/light sour, 2% acidic sweet, 16% otherCapable of processing imported intermediate feedstocks Primary utilities used include natural gas, electric power and fresh water

California gasoline CARBOB80% CARBOB distributed through pipeline system20% finished gasoline blended at Refinery terminalMajor supplier of Military jet fuel in northern California (pipeline)Refinery also produces EPA diesel fuel (pipeline)Ultra Low Sulfur Diesel (ULSD)Unit nearing completionFlexible light-ends system allows for a variety of propane and butane dispositions and minimizes external natural gas purchases (LPGs shipped by rail and truck) Benicia Asphalt Plant supplies 25% of northern California asphalt market (shipped by truck)

$484 MM invested in capital improvements and $233 MM for turnaround maintenance at Benicia since Valero acquisition Ultra Low Sulfur Diesel Unit (ULSD) $105 MMConstructing New Crude Tanks (2 650 MB) $60 MM Major plant-wide turnaround completed in 4Q2004 Alky expansion project commissioned in the 1Q2004 -eliminated need to export pentanes or import high octane, low vapor pressure blendstocks $25 MMMTBE phase-out 2003 $25 MM51 MW cogeneration facility completed in 2002 $60 MM

Valero Improvement Project (VIP)development under way for 2010 turnaround and beyondCrude Sour-up to reduce dependence on ANSNew desalterSulfur removal and sulfur recovery capacity improvementsFlue gas scrubber for Coker and FCCNew hydrogen manufacturing unitImproved energy efficiencyGreenhouse Gas (GHG)reduction

Depending on refinery configuration, CARBDepending on refinery configuration, CARB gasoline pool could be reduced by 2% to 4%gasoline pool could be reduced by 2% to 4% net of ethanol net of ethanolModel changes drive increase in ethanol content from 5.7% to 10% by volume Sulfur content must be reduced to accommodate NOx increases from ethanol Sulfur reductions require additional hydrotreating of FCC gasoline Aromatics change reduces reformate blending and FCC gasoline cut points, which increases need for alkylate and raffinate

Appendix

DefinitionSeparating crude oil into different hydrocarbon groupsThe most common means is through distillationProcessDesalting Prior to distillation, crude oil is often desalted to remove corrosive salts as well as metals and other suspended solids.Atmospheric Distillation Used to separate the desalted crude into specific hydrocarbon groups (straight run gasoline, naphtha, light gas oil, etc.) or fractions.Vacuum Distillation Heavy crude residue (bottoms) from the atmospheric column is further separated using a lower-pressure distillation process. Means to lower the boiling points of the fractions and permit separation at lower temperatures, without decomposition and excessive coke formation.

DefinitionCracking or breaking down large, heavy hydrocarbon molecules into smaller hydrocarbon molecules thru application of heat (thermal)or through the use of catalystsProcessCoking Thermal non-catalytic cracking process that converts low value oils to higher value gasoline, gas oils and marketable coke. Residual fuel oil from vacuum distillation column is typical feedstock.Visbreaking Thermal non-catalytic process used to convert large hydrocarbon molecules in heavy feedstocks to lighter products such as fuel gas, gasoline, naphtha and gas oil. Produces sufficient middle distillates to reduce the viscosity of the heavy feed.Catalytic Cracking A central process in refining where heavy gas oil range feeds are subjected to heat in the presence of catalyst and large molecules crack into smaller molecules in the gasoline and surrounding ranges.Catalytic Hydrocracking Like cracking, used to produce blending stocks for gasoline and other fuels from heavy feedstocks. Introduction of hydrogen in addition to a catalyst allows the cracking reaction to proceed at lower temperatures than in catalytic cracking, although pressures are much higher.

DefinitionLinking two or more hydrocarbon molecules together to form a large molecule (e.g. converting gases to liquids) or rearranging to improve the quality of the moleculeProcessAlkylation Important process to upgrade light olefins to high-value gasoline components. Used to combine small molecules into large molecules to produce a higher octane product for blending with gasoline.Catalytic Reforming The process whereby naphthas are changed chemically to increase their octane numbers. Octane numbers are measures of whether a gasoline will knock in an engine. The higher the octane number, the more resistance to pre or self-ignition.Polymerization Process that combines smaller molecules to produce high octane blending stock.Isomerization Process used to produce compounds with high octane for blending into the gasoline pool. Also used to produce isobutene, an important feedstock for alkylation.

DefinitionProcessing of petroleum products to remove some of the sulfur, nitrogen, heavy metals, and other impuritiesProcessCatalytic Hydrotreating, Hydroprocessing, sulfur/metals removal Used to remove impurities (e.g. sulfur, nitrogen, oxygen and halides) from petroleum fractions. Hydrotreating further upgrades heavy feeds by converting olefins and diolefins to parafins, which reduces gum formation in fuels. Hydroprocessing also cracks heavier products to lighter, more saleable products.

AGO Atmospheric Gas Oil kVA Kilovolt Amp ATB Atmospheric Tower Bottoms LCO Light Cycle Oil B-B Butane-Butylene Fraction LGO Light Gas OilBBLS Barrels LPG Liquefied Petroleum Gas BPD Barrels Per Day LSD Low Sulfur Diesel BTX Benzene, Toluene,Xylene LSR Light Straight Run (Gasoline) CARB California Air Resource Board MON Motor Octane Number CCR Continuous Catalytic Regenerator MTBE Methyl Tertiary-Butyl Ether DAO De-Asphalted Oil MW Megawatt DCS Distributed Control Systems NGL Natural Gas Liquids DHT Diesel Hydrotreater NOX Nitrogen Oxides DSU Desulfurization Unit P-P Propane-Propylene EPA Environmental Protection Agency PSI Pounds per SquareInchESP Electrostatic Precipitator RBOB Reformulated Blendstock for Oxygen Blending FCC Fluid Catalytic Cracker RDS Resid Desulfurization GDU Gasoline Desulfurization Unit RFG Reformulated Gasoline GHT Gasoline Hydrotreater RON Research Octane Number GOHT Gas Oil Hydrotreater RVP Reid Vapor Pressure GPM Gallon Per Minute SMR Steam Methane Reformer (Hydrogen Plant) HAGO Heavy Atmospheric Gas Oil SOX Sulfur Oxides HCU Hydrocracker Unit SRU Sulfur Recovery Unit HDS Hydrodesulfurization TAME Tertiary Amyl Methyl Ether HDT Hydrotreating TAN Total Acid Number HGO Heavy Gas Oil ULSD Ultra-low Sulfur Diesel HOC Heavy Oil Cracker (FCC)VGO Vacuum Gas Oil H2 Hydrogen VOC Volatile Organic Compound H2S Hydrogen Sulfide VPP Voluntary Protection Program HF Hydroflouric (adic)VTB Vacuum Tower Bottoms HVGO Heavy Vacuum Gas Oil WTI West Texas Intermediate kV Kilovolt WWTP Waste Water Treatment Plant

Statements contained in this presentation that state the Companys or managements expectations or predictions of the future are forward-looking statements intended to be covered by the safe harbor provisions of the Securities Act of 1933 and the Securities Exchange Act of 1934. The words believe, expect, should, estimates, and other similar expressions identify forward-looking statements. It is important to note that actual results could differ materially from those projected in such forward-looking statements. For more information concerning factors that could cause actual results to differ from those expressed or forecasted, see Valeros annual reports on Form 10-K and quarterly reports on Form 10-Q, filed with the Securities and Exchange Commission, and available on Valeros website at www.valero.com.

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