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6 th - PPT Presentation

European Middle Distillates Conference January 26 27 2016 Direct Extraction DX Technology Middle Distillate Desulfurization WHY DESULFURIZATION Increase Marketability ID: 613435

ppm desulfurization design cost desulfurization ppm cost design technology sulfur diesel 4900 amp operating roles hds process dxs distillate

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Slide1

6th European Middle Distillates ConferenceJanuary 26 – 27, 2016Direct Extraction (DX) TechnologyMiddle Distillate DesulfurizationSlide2

WHY DESULFURIZATION?Increase Marketability Higher Fuel ValueExpand MarketsHigh Value Sulfur By-Products

The Importance of

Middle Distillate Desulfurization Slide3

New TechnologyWhy the need for new technology on Desulfurization?Complementary and alternative to conventional desulfurization technology:Simpler and less expensive DX processLower operating costsMore dependable and cost competitive Desulfurization Process based on simple packbed adsorption processDebottleneck existing plants

Benefit of New Desulfurization Technology

To offset profit lossSlide4

Flow SheetSlide5

Packaged skid-mounted equipmentStandard design and quick deliveryVarious standard sizes- 500 to 20,000 BPD modules“Plug & Play”DX DesignSlide6

DX RolesSlide7

DX RolesSlide8

DX RolesSlide9

Mass BalanceSlide10

DXs Technology on Diesel with 4900 ppm & 2900 ppm SulfurOperational ResultsFull scale pilot plantSlide11

Test ResultsGraph illustrates the DXs process in untreated (non-oxidized) diesel from 4900 pp to 10 ppm.DXs process removes the same species of organosulfur compounds from the highly concentrated 4900 ppm sulfur diesel to the same extent as from the less concentrated 300 ppm sulfur dieselOrganoSulfur MarkersSlide12

Operating Costs of HDS, ODS and DXCost ofHydro DesulfurizationOxidative DesulfurizationDirect ExtractionPressure and TemperatureHighLowLowCatalyst / AdsorbentModerateHighModerateMaintenanceHigh

High

Low

EquipmentHighHighModerateSafety ManagementHigh

High

Low

Economic Analysis on

Current TechnologiesSlide13

Hydro DesulfurizationOxidative DesulfurizationDirectExtractionCapital CostUS $ 24mUS $ 21mUS $10mHydrogen US $ 17.2m/yearN/AN/APeroxideN/A

US

$

12.6m/yearN/AOperating CostUS $ 22.4m/yearUS $ 20.8m/yearUS $ 5.2m/year

Operating Cost

per Barrel

$1.79

$1.61

$0.45

*https

://web.anl.gov/PCS/acsfuel/preprint%20archive/Files/49_2_Philadelphia_10-04_1055.pdf

Cost Analysis per 30,000 BPD*Slide14

Packaged design for quick installationIncrease fuel value & marketabilityStand-alone processing or optimization of current HDS facilitiesLower operating costDebottleneck existing HDS capacityFlexibility of Design to meet 500 ppm middle distillate or 10 PPM ULSDSummarySlide15

Questions

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