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Increasing Revenues in Resid FCC<br />

Carel Pouwels, Ken Bruno, Yen Yung, Eelko Brevoord<br />

ERTC 2011<br />

December 6, 2011


Content<br />

Introduction<br />

– Trends in RFCC<br />

Introducing UPGRADER TM<br />

– <strong>Albemarle</strong>’s Solutions for Processing More Residue<br />

– Maximum upgrading at lowest Rare Earth<br />

UPGRADER EXPERIENCE<br />

– Cases of UPGRADER applications<br />

Low Rare Earth <strong>Technology</strong> (LRT TM )<br />

– <strong>Albemarle</strong>’s Solution for Processing More Residue at lowest Rare Earth<br />

Summary and Conclusions<br />

2


1.0<br />

Introduction<br />

Trends in Processing Residue in FCC<br />

3


Crude Toward Heavier and Higher Sulfur<br />

33<br />

1.8<br />

Gravity<br />

Crude Gravity ( °API)<br />

32<br />

31<br />

30<br />

Sulfur<br />

1.6<br />

1.4<br />

1.2<br />

Sulfur (wt%)<br />

29<br />

1995 2000 2005 2010 2015 2020<br />

1.0<br />

Source: Hart World Refining and Fuels Service<br />

4


Customer’s Requirements<br />

Cost Reduction<br />

– Cheaper (heavier) feeds: increased intake of resid<br />

– Lower catalyst cost per ton feed: enhanced metal resistant catalysts<br />

• Strong driver today: maximize upgrading at lowest RE2O3<br />

Value Enhancement<br />

– Increased conversion (activity)<br />

– Upgrading to more valuable products<br />

5


In resid applications, improved bottoms<br />

conversion, lower coke or a balance between<br />

both is usually most economic.<br />

6


The Complex Chemistry of Coke Formation<br />

Upgraded Products<br />

Feed<br />

Condensation<br />

Alkylation<br />

Cyclization<br />

Aromatization<br />

Polymerization<br />

Hydrogen Transfer<br />

Coke Precursors<br />

Hydrogen Transfer<br />

Dehydrogenation<br />

Coke<br />

7


Feed Coke and Metals Coke Dominate When Processing<br />

Resid<br />

70%<br />

60%<br />

50%<br />

Delta Coke Contribution by Coke Type<br />

Gas Oil<br />

Resid<br />

40%<br />

30%<br />

20%<br />

10%<br />

0%<br />

Catalytic Stripping Feed Metals<br />

8


<strong>Albemarle</strong>’s Matrices: Tunable for Heavy Molecules Pre-<br />

Cracking and Low Coke Selectivity<br />

Pre-cracking of heavy molecules by<br />

matrix<br />

Metals encapsulation/ trapping/<br />

passivation by matrix<br />

High Accessibility Structure<br />

– Allows large heavy feed<br />

molecules access to the active<br />

sites<br />

– Allows products to leave<br />

without undergoing secondary<br />

reactions<br />

High pore volume and high cracking<br />

activity<br />

heavy<br />

oil<br />

binder<br />

matrix<br />

gasoline<br />

zeolite<br />

model<br />

FCC catalyst model<br />

9


Designing a Max Resid Catalyst<br />

Requirements<br />

– Good bottoms cracking for slurry conversion and low “feed coke”<br />

– Metals tolerance for activity and low “metals coke”<br />

– Optimize Hydrogen Transfer to limit “catalytic coke” and desired<br />

balance between LPG and gasoline<br />

– Open pore structure for low “stripping coke”<br />

Design Parameters<br />

– Matrix: Pre-cracking large molecules, metals tolerance, low hydrogen<br />

transfer<br />

– High Accessibility: high pre-cracking/low secondary reactions as<br />

hydrogen transfer, condensation, polymerization, etc.<br />

– Zeolite: activity, selectivity<br />

– RE2O3: critical for resid<br />

10


High accessibility, effective bottoms cracking matrix<br />

with tunable metals resistance and coke selectivity<br />

and greater zeolite activity and stability are key.<br />

11


2.0<br />

Introducing UPGRADER TM<br />

<strong>Albemarle</strong>’s Solutions for Processing More Residue<br />

12


<strong>Albemarle</strong>’s Solutions for Processing More Residue<br />

UPGRADER TM : Lowest slurry in the industry<br />

UPGRADER R+: Max bottoms conversion for delta coke limited operations<br />

CORAL TM (SMR): Lowest coke selectivity<br />

AFX TM : Maximum C3=<br />

13


UPGRADER TM<br />

Lowest Slurry in the Industry<br />

Premium Resid Catalyst<br />

– Utilizes improved manufacturing technology that permits higher AAI, better coke<br />

selectivity, and expanded formulation window<br />

• Succeeds previous OPAL TM catalyst family, known for its industry leading slurry<br />

conversion<br />

Applications:<br />

– Resid feedstocks<br />

– Cracking bottom of the barrel<br />

– Diffusion constraint situations<br />

– High V, Ni, Fe and/or Ca feeds<br />

14


UPGRADER TM<br />

Lowest Slurry in the Industry<br />

Catalytic Features:<br />

– Highest AAI in the industry<br />

– Greater zeolite activity and stability<br />

– Most effective bottoms cracking matrix with tunable metals tolerance and coke<br />

selectivity<br />

Potential Benefits:<br />

– Lowest slurry in the industry<br />

– Lower coke selectivity<br />

– Max transportation fuels, tunable toward more gasoline or more LCO<br />

– Increased throughput<br />

– Increased olefinicity/octane<br />

15


UPGRADER TM R+<br />

Max Bottoms Conversion for Delta Coke Limited Operations<br />

Application:<br />

– Same as UPGRADER but where better coke selectivity is required in the unit<br />

Features:<br />

– Improved coke selectivity (more coke selective matrix) vs. UPGRADER<br />

– Improved accessibility and V, Fe, Ca tolerance (vs. CORAL TM )<br />

Potential Benefits:<br />

– More resid processing than UPGRADER for delta coke limited units<br />

– More bottoms destruction vs. CORAL<br />

16


3.0<br />

UPGRADER TM EXPERIENCE<br />

Cases of UPGRADER Applications<br />

17


UPGRADER TM<br />

Refiner Needs to Reduce Bottoms of the Barrel<br />

Resid FCC Unit:<br />

– Specific Gravity: 0.90<br />

– Sulfur: 0.6 wt%<br />

– Conradson Carbon: 3.5 wt%<br />

– Nitrogen: 700 ppm<br />

Catalyst:<br />

– Base catalyst: Competitive coke selective resid catalyst<br />

– Activity: 64 w%<br />

– Ni/V = 4000/6500 ppm<br />

Refiners Objective:<br />

– Bottoms cracking<br />

18


UPGRADER TM<br />

Massive Upgrading Potential of UPGRADER Demonstrated<br />

6<br />

Delta Yield, UPGRADER - COMPETITOR<br />

60%<br />

4<br />

40%<br />

Yield benefits, wt%<br />

2<br />

0<br />

-2<br />

20%<br />

0%<br />

-20%<br />

Catalyst benefits, %<br />

-4<br />

-40%<br />

-6<br />

Gasoline LCO Slurry Conversion CAR AAI<br />

-60%<br />

19


UPGRADER TM<br />

Massive Upgrading Potential of UPGRADER Demonstrated<br />

Competitor<br />

UPGRADER<br />

Operating Conditions:<br />

Feed Rate m³/h Base Base<br />

Rx Outlet T °C 516 510<br />

Rg Bed T °C 732 734<br />

CTO 4.8 4.3<br />

Delta Coke wt% 1.3 1.4<br />

CAR mt/d 7.6 7.0<br />

Ecat Quality:<br />

Activity wt% 63.0 64.4<br />

AAI Base + 50%<br />

Yields:<br />

Dry Gas (incl. H2S) wt% 2.6 2.4<br />

LPG wt% 11.3 10.7<br />

Propylene wt% 2.8 2.7<br />

Total C4 wt% 7.6 7.2<br />

Gasoline (C5-221C) wt% 41.4 44.0<br />

LCO (221-400C) wt% 26.2 28.4<br />

Slurry wt% 12.4 8.4<br />

Coke wt% 6.0 6.1<br />

Conversion wt% 61.4 63.2<br />

* Normalized to equal feed quality, throughput and metals on Ecat<br />

20


UPGRADER TM R+<br />

Commercial Experience in UOP SBS Unit<br />

Unit design: UOP SBS<br />

Conditions: see table<br />

Base catalyst: CORAL SMR (lowest<br />

delta coke catalyst for resid)<br />

Refiners objectives:<br />

– Process more resid (improved<br />

coke selectivity)<br />

– Improved bottoms conversion<br />

Feed Quality<br />

Base case<br />

Density g/cm 3 0.912<br />

CCR wt% 1.5<br />

Operating Conditions<br />

Feed Rate, m3/h m 3 /h Base<br />

RXT °C 522<br />

RGT °C 716<br />

Fresh cat additions t/d 4<br />

CTO 6.6<br />

E-cat<br />

Activity wt% 70<br />

Ni ppm 2132<br />

V ppm 2539<br />

21


UPGRADER TM R+<br />

Combines Improved Bottoms Cracking with Low Coke Yield<br />

UPGRADER R+ is a smashing success:<br />

– enhanced metals resistance to improve coke selectivity: RgT decreased by 7 o C<br />

– more effective bottoms cracking matrix<br />

Leading to impressive conversion increase, slurry reduction and MON barrels uplift<br />

CORAL SMR UPGRADER R+<br />

Yields<br />

Fuel Gas wt% Base -0.2<br />

LPG wt% Base 2.0<br />

C3= wt% Base 0.7<br />

iC4= wt% Base 0.3<br />

iC4 wt% Base 0.5<br />

Gasoline wt% Base 1.5<br />

LCO wt% Base 0.2<br />

Slurry wt% Base -3.5<br />

Coke wt% Base 0.1<br />

Conversion wt% Base 3.3<br />

Product Properties<br />

C4 olefinicity Base 0.02<br />

MON Base 1.0<br />

22


4.0<br />

Low Rare Earth <strong>Technology</strong> (LRT TM )<br />

<strong>Albemarle</strong>’s Solutions for Processing More Residue at Lowest Rare Earth<br />

23


Why do we Need Rare Earth in FCC Catalysts?<br />

Why does <strong>Albemarle</strong> Need Less Rare Earth than Competition?<br />

Zeolite is the most active component in FCC catalysts<br />

This zeolite needs to be stabilized against steam deactivation at high regenerator<br />

temperatures<br />

Rare earth exchange is the most effective method to stabilize zeolite<br />

However, there are also disadvantages from RE:<br />

– Poorer coke selectivity<br />

– Lower LPG olefins and gasoline octanes<br />

It has always been <strong>Albemarle</strong>’s strategy to achieve optimum zeolite stability with less RE.<br />

This way, negative effects of RE on performance are minimized.<br />

<strong>Albemarle</strong>’s average rare earth content is the lowest<br />

After the recent RE price increase, there is an appreciable reduction in catalyst costs due<br />

to the lower RE on <strong>Albemarle</strong> catalysts.<br />

– Example: 4 tpd, 1 wt% lower RE => $ 1.6 million per year<br />

24


<strong>Albemarle</strong> offers a proven family of Low Rare Earth<br />

<strong>Technology</strong> (LRT TM ) based Catalyst and Additives,<br />

which have been supplied commercially.<br />

25


<strong>Albemarle</strong>’s LRT <strong>Technology</strong>: Proven Family of Low Rare<br />

Earth <strong>Technology</strong> Based on Catalysts and Additives<br />

Makes use of a combination of proven technologies<br />

– ADZT-200 zeolite treatment: Gives activity and RE-selectivity at lower RE levels<br />

– High zeolite content<br />

– High Silica to alumina (SAR) Y-zeolites: Extra stability!<br />

– High matrix power (highest in industry)<br />

– High accessibility: Better utilization of zeolite and matrix<br />

– Metals tolerant and trapping technologies (non-RE-based)<br />

We believe a minimum level of RE is required for optimum stability and cost/day<br />

12<br />

Delta Activity, wt%<br />

10<br />

8<br />

6<br />

4<br />

2<br />

0<br />

2% Activity Increase with ADZT-200<br />

Standard Zeolite<br />

ADZT-200 Zeolite<br />

First 0.5 – 0.7% rare earth oxide is optimal<br />

0 1 2 3 4 5<br />

RE2O3 on Catalyst, wt%<br />

26


<strong>Albemarle</strong>’s LRT TM Solutions for Resid Applications<br />

UPGRADER TM LRT:<br />

CORAL TM LRT:<br />

BCMT - 500 LRT:<br />

Lowest slurry resid catalyst at low Rare Earth<br />

Lowest coke resid catalyst at low Rare Earth<br />

Low Rare Earth<br />

Feed<br />

Gas Oil<br />

Residue<br />

Desired<br />

Output<br />

Gasoline/Conversion<br />

Maximum<br />

Bottoms Cracking<br />

AMBER TM<br />

AMBER LRT TM<br />

UPGRADER TM<br />

UPGRADER LRT TM<br />

LCO<br />

Lowest Coke C3= Octane/C4=<br />

GO-Ultra TM<br />

GO LRT TM<br />

UPGRADER R+ TM<br />

CORAL TM<br />

CORAL LRT TM<br />

AMBER MD TM<br />

UPGRADER MD<br />

Octane/Olefins<br />

AFX TM<br />

AFX TM<br />

ACTION TM<br />

ACTION TM<br />

27


UPGRADER LRT Increases Profitability in R2R Unit<br />

Competitor UPGRADER TM LRT<br />

Operating Conditions<br />

Feed Rate BPD Base Base + 3000<br />

Feed API 27.4 25.8<br />

CCR, wt % 1.0 1.0<br />

% VTB 14 17<br />

Preheat Deg F 473 460<br />

Riser Deg F 985 985<br />

Regen Dense Deg F 1334 1323<br />

Ecat Properties<br />

Activity, wt % 65 65<br />

RE2O3 wt % 2.30 0.85<br />

Catalyst Addition Rate Base Base<br />

Matrix Surface Area, m2/gm 37 83<br />

AAI 2 7<br />

FCCU Yields<br />

C2 Minus, scfb 406 330<br />

LPG, vol % 20.8 19.6<br />

C3=/TC3 0.75 0.76<br />

C4=/TC4 0.56 0.64<br />

Gasoline, vol % 52.9 62.5<br />

LCO, vol % 19.4 20.9<br />

Slurry, vol % 16.4 8.2<br />

Slurry API 12.9 4.2<br />

Conversion, vol % 64.2 70.9<br />

Profitability Base > $20 Million/year<br />

RE2O3 = 0.85<br />

– Maintains activity<br />

– Superior performance<br />

LRT Options employed:<br />

– Higher matrix<br />

– Higher AAI<br />

Large yield benefits<br />

– Above Critical AAI<br />

Greater than $20MM/yr<br />

increased profitability<br />

28 28


5.0<br />

Summary and Conclusions<br />

29


UPGRADER TM and LRT TM<br />

Summary and Conclusions<br />

UPGRADER: The ultimate catalyst for converting resid<br />

UPGRADER R+: For delta coke limited applications<br />

– Advanced matrix components<br />

– Highest matrix activity, as needed<br />

– High AAI <strong>Technology</strong><br />

– Metals trapping technology, as needed<br />

LRT products deliver maximum activity and performance per rare earth<br />

– ADZT-200 Zeolites<br />

– High zeolite loading, high SAR zeolites<br />

– Optimized manufacturing technology<br />

<strong>Albemarle</strong>’s average Rare Earth is the lowest<br />

30

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