May 15, 2017May 17, 2017

Cairo, Egypt Alexandria, Egypt

Hydrocracking InnovationsUOP Technologies for Distillate ProductionErik Svensson

Hydroprocessing and Heavy Oil

Technology Manager2017 Honeywell Oil & Gas Technologies Symposium

0

40 000

80 000

120 000

160 000

200 000

1950 1955 1960 1965 1970 1975 1980 1985 1990 1995 2000 2005 2010 2015 2020

Lic

en

se

d C

ap

ac

ity,

BP

SD

Award Year

Unionfining Units Unicracking Units

64 Years in Hydroprocessing Innovations

340+ Unionfining Units & 220+ Unicracking Units Licensed

1

Unity

HydroprocessingCatalysts

TM

UOP 7432D-1

19521st UnionfiningTM

Unit

19601st

UnicrackingTM

Unit

1990s 2006

HPNA Management

2008 E2S Process

2016

2012UniflowTM Reactor

Internals

4th Generation

2011ExxonMobil

Lubes & Fuels Alliance

UOP Hydroprocessing

Experience

Distillate

LCO

VGO

CGO

DAO

Hydrocracking Technology Portfolio

2

Customized Solutions to Meet Customer Objectives

Naphtha

Kero/Jet Fuel

Diesel Fuel

Lubes EMCL MSDWTM &

MAXSATTM Technology

Single Stage Recycle

HPNA Management

Dual Stripper/Dual Frac

Feedstock ProductsUnicracking

Fractionation SectionUnicracking

Reactor Section

TwoStage Recycle

Once Through

3

Portfolio of Multiple Solutions

Heavy Oil Processing

Honeywell Process Control Solutions

Distillate Dewaxing and Lube

Base Oil Production

Crystaphase CatTrap

UOP 7432D-3

UOP Uniflex Process

4

Operational Needs

Maintaining Throughput

End of Run

Maintaining Yields

Maintaining Product Qualities

Long Term

Increased Throughput

UCO Utilisation

High Conversion

Improved Energy Efficiency

Greater Product Recovery

Next Cycle

Reactor Performance

Opportunity Feedstocks

Product Slate Flexibility

Enhanced Product Qualities

Improved Product Yield

Improved Profitability and Flexibility

UOP 7432D-4

Next Cycle Opportunities

• Catalyst Selection - Increased Yields

- Improved Product Qualities

• Increased Conversion- HPNA Management

• Improved Reactor Performance- Reactor Replacements

Opportunities for improved operation

- Uniflow Reactor Internals Reduced quench zone height

Shorter installation time

Easier maintenance

Improved Distribution

5

Improved Product Yield Increased Cycle Increased Conversion

UOP 7432D-4

Example: Installed in 5-bed HC reactor in

Nov, 2014. Unit operating at 32% higher

feed rate compared to previous cycle.

• New design offering a step change in performance & speed of installation

• First sale in 2013

• Sold into 20 units (new and revamp) with 10 operating successfully

6Improved Distribution with UOP Uniflow Reactor Internals

Customer Feedback:

Hydrocracking

Bed

Radial Spread (ºF)

New Cycle

Radial Spread (ºF)

Previous Cycle

Bed 1Top: 1

Bottom: 1

Top: 3

Bottom: 18

Bed 2Top: 4

Bottom: 3

Top: 2

Bottom: 6

Bed 3Top: 4

Bottom: 2

Top: 5

Bottom: 6

Bed 4Top: 4

Bottom: 3

Top: 12

Bottom: 36

Bed 5Top: 4

Bottom: 4

Top: 11

Bottom: 45

“We would never have been able to operate this unit where it is today without these new internals.

This is a step change for UOP”

UOP 7432D-6

UOP UniflowTM Reactor Internals

7

UOP 7432D-7

MIDOR Refinery Expansion ProjectBoosting Refinery Capacity – 100,000 to 160,000 BPSD

Project Objectives

• Refinery throughput increased 60%

• Maximising middle distillate yield

• Meet future legislation of high

quality EuroV specifications

• Zero fuel oil production

Additional Requirements

• Maximum utilisation of existing

refinery units

• Minimise refinery downtime

• Limited plot space

8

UOP 7432D-10

MIDOR Refinery Expansion ProjectBoosting Refinery Capacity – 100,000 to 160,000 BPSD

9

UOP 7432D-9

Coke

Euro VDiesel

LocalDiesel

Kerosene

Euro VGasoline

R95

LPGSGP LPG

MeroxLPGFrac.

NHT

DelayedCoker

SDA

CDU

CDU

NS

HC LPG

LPG Fuel GasC3/C4

IsomerateISOM

Reformate

CCR

LPG from other unitsCDU LPG

CrudeOil

SRN

Kero

SRD

CDU LPG

At Res

VGO

SRN

Kero

CrudeOil

KHTNAP

SRD

VDU

At Res VGO

Pitch

HCGO

DCNAP

VDU

HC NAP

HC LPG to LPG Frac

DHT NAP

HT Diesel

DAO

HC Diesel

HC KeroHC

NewDHT

LCGO

KHT

New Unit

Revamp

Existing Unit

UCO

MIDOR Refinery Expansion ProjectCurrent Kerosene and Diesel Processing Configuration

10

Existing DHT29,000 BPSD

Local Diesel

50 wtppm S

Jet A1

Existing Kerosene

Merox11,000 BPSD

Current Configuration

• Targets local diesel production

• Kerosene to Jet A1 pool only

• No ability to achieve EuroV diesel specifications

UOP 7432D-12

SR Diesel + LCGO

SR Kerosene

MIDOR Refinery Expansion ProjectMaximising Euro V Diesel Production

11

KHT

(Revamped DHT)18,000 BPSD

Local Diesel

50 wtppm S

Euro V Diesel

10 wtppm S

Jet A1

SR Kerosene

Existing Kerosene

Merox11,000 BPSD

SR Kerosene

New DHT48,000 BPSD

SR Diesel + LCGO

Ultimate flexibility between Jet A1 and EuroV Diesel production. Minimum shutdown and plot space

with optimised investmentUOP 7432D-13

12

Separation Fractionation

33,000 BPSD

VGO+HCGO

Make-up Gas

17,000 BPSD

Naphtha

Kerosene

Diesel

UCO

Unicracking Unit

Existing Configuration

UOP 7432D-14

13

Separation Fractionation

35,000 BPSD

UCO

Make-up Gas

Naphtha

Kerosene

Diesel

New RG Scrubber

Separation Fractionation

HPNA Management

MUG

Naphtha

Kerosene

Diesel

UCO

Common H2

Recovery

Unicracking Unit

New Configuration

Uniflow Reactor

Internals

UOP 7432D-113

50,000 BPSD

VGO+HCGO+DAO

MIDOR Refinery Expansion ProjectBoosting Refinery Capacity – 100,000 to 160,000 BPSD

• Investment cost of $1.8 billion

• EPC Phase expected to commence 4th quarter 2017

• Internal rate of return 30% confirming the economic

importance of the expansion.

14

Product % Increase

LPG 84%

High Octane Gasoline 52%

Jet Fuel 180%

Diesel 33%

Total Distillate 75%

UOP 7432D-16

• Industry-leading hydrocracking technology for optimizing the production of high quality fuels

• Multiple solutions for next cycle and long term opportunities strategies:

- Hydrocracking innovations

- Bottom of the barrel upgrading

- Alliances

- Honeywell process solutions

• Flexible offerings to meet refiners’ processing and financial objectives

• Focus on innovation to improve hydroprocessing performance and reduce capital and operating costs

• UOP can evaluate the product slate, capital expense and operating expense of the overall complex to provide the highest value solution to the customer

Solutions for Improved Hydrocracking PerformanceImproved Profitability and Flexibility

15

Combining cutting-edge design and 65 years of experience to deliver maximum valueUOP 7432D-17

16

UOP 7432D-16