ADVANCES IN REFORMING CATALYST - World · PDF file1 ADVANCES IN REFORMING CATALYST....

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1 ADVANCES IN REFORMING CATALYST International Refining Seminar Refining Challenges and Way Forward” Organised by Petroleum Federation of India 16 th -17 th April, 2012 New Delhi (India) Mohan Lal Axens India

Transcript of ADVANCES IN REFORMING CATALYST - World · PDF file1 ADVANCES IN REFORMING CATALYST....

Page 1: ADVANCES IN REFORMING CATALYST - World · PDF file1 ADVANCES IN REFORMING CATALYST. International Refining Seminar “ Refining Challenges and Way Forward” Organised by Petroleum

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ADVANCES IN REFORMING CATALYSTInternational Refining Seminar

“Refining Challenges and Way Forward”Organised by Petroleum Federation of India

16th -17th April, 2012 New Delhi (India)

Mohan LalAxens India

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March 2011 Acquisition of the reforming business of Criterion corporation

Salindres, FranceWillow Island, West Virginia, USA

• Each Heritage catalyst produced within heritage organization

• On-going cross production trials• Different paths lead to quality products: mechanical strength,

hydrothermal stability, chlorine retention

• Great improvement potential from experience sharing

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Merger status

• Current situation• Axens & Criterion legacy products still available

• On going process for • Portfolio consolidation• New products launching

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What do Customers Look For ?

• Proven and reliable catalyst

Axens’ SolutionsHomologated by MajorsMore than 200 references with

promoted catalyst

Customer Targets

Optimal Pt content & Loading density

Minimised side reactionsUse of promoted catalyst

• Improved economics

High chloride retentionHigh mechanical resistance

Stable surface area Stable platinum dispersionLow coke make catalyst

• High Stability

• Low cost-to-fill • High hydrogen & Reformate

production or aromatics production

• Low operating cost

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Fixed Bed Reforming Catalysts

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TA 1 – CR 607 Client technical assistance

• Current portfolio

• New products

• Development

• Summary

• Reactor technology

SR & Cyclic section

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Fixed Bed Reforming Catalysts Established Products

Re / Pt 0 1 1.3 1.6 1.8

Target Unit CY SR/CY SR/CY SR SR

Increased Stability

Better S tolerance

Unconstrained Unit

Increased Activity

Higher Density

The largest family of Multi-Promoted Fixed Bed Catalysts

RG 532 RG 582 RG 682

P 15 PR 15 PR 30

RG 586

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Fixed Bed Reforming Catalysts New Products

Re / Pt 0 1 1.3 1.6 1.8

Target Unit CY SR/CY SR/CY SR SR

Increased Stability

Better S tolerance

Unconstrained Unit

Increased Activity

Higher Density

The largest family of Multi-Promoted Fixed Bed Catalysts

PR 33 PR 36

New New

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Fixed Bed Reforming Catalysts Available Products

Re / Pt 0 1 1.3 1.6 1.8

Target Unit CY SR/CY SR/CY SR SR

Increased Stability

Better S tolerance

Unconstrained Unit

Increased Activity

Higher Density

The largest family of Multi-Promoted Fixed Bed Catalysts

RG 532 RG 582 RG 682

P 15 PR 15 PR 33 PR 36 PR 30

RG 586

New New

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TA 1 – CR 607 Client technical assistance

• Current portfolio

• New products

• Development

• Summary

• Reactor technology

SR & Cyclic Section

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New Reforming Catalysts

P/N/A = 60/24/13 % wt

PR 33 PR 36 ; PR 30PR 15• Higher catalyst stability

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New Reforming Catalysts

• Higher yields stability

PR 36 ; PR 30

PR 15

P/N/A = 60/24/13 % wt

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Outcome

• The PR 33 & PR 36 catalysts provide

• High catalyst performances• Selectivity & stability • Fully regenerable

• At the lowest precious metal content• The highest NPV for fixed bed application

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TA 1 – CR 607 Client technical assistance

• Current portfolio

• New products

• Development

• Summary

• Reactor technology

SR & Cyclic Section

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Nearing Commercialization

• The highest selectivity with a maximum C8 aromatics production at constant catalyst activity

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Fixed Bed Reforming Catalysts New Products

Re / Pt 0 1 1.6

Target unit CY SR/CY SR

Increased stability

Better S tolerance

Higher density

The new family of multipromoted

catalyst

P 152 PR 150 PR 156

We call them PR as we initially focus on high density carrier

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New Series Balanced version

490

495

500

505

510

515

520

525

530

0 24 48 72 96 120 144 168 192 216 240 264 288

Time (hours)

Norm T, Deg C PR 15 New

Same activity but higher stability20 % less coke

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New Series Balanced version

PR 15 NewH2

(wt %)Base +0.1

H2(scfb)

Base +60

C5+

(wt %)Base +1.5

82

83

84

85

86

87

88

48 72 96 120 144 168 192 216 240 264 288

Time (hours)

Normalized C5+, wt % PR 15 New

Max selectivity catalyst

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New Series Balanced version

29.0

29.5

30.0

30.5

31.0

31.5

32.0

48 72 96 120 144 168 192 216 240 264 288

A8, wt %

PR 15 NewA6

(wt %)

Base Base

A7

(wt %)

Base +0.51

A8

(wt %)

Base +0.67

Time (hours)

PR 15 New

Higher C8

aromatics yield catalyst

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Axens Fixed Bed Catalyst Advantages

• RG/PR catalysts are used by majors oil companies• More than 200 references with promoted catalyst

• Loading density adjusted to comply with customer needs• The highest selectivity

• Fixed bed reforming catalysts are Pt / Re based therefore in order to change the yields we need to add something new

Promoted catalyst

• The highest stability • Pt sintering hindered with promoter

• Longer cycles • Outstanding surface stability

• Longer life

• The highest chloride retention

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• Side reactions• Hydrocracking linked to very acidic sites

• Modified carrier

• Hydrogenolysis linked to metal activity• Modified metals function

• Promoter serves 2 roles • Lower C3 & C4 production• Lower C1 & C2 production

Higher hydrogen and C5+ yields

Axens Fixed Bed Catalyst Advantages Selectivity

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CCR Reforming

Catalysts

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CCR Development Methodology

• For 30 years the CCR catalyst market has been almost fully dominated by Pt/Sn• Any improvements maintaining the same formulation is very

difficult

• The market still wants higher yields• Mainly hydrogen• Mainly aromatics

Need for new catalyst formulation

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Prerequisite for the Formulation

• The formulation needs• To be fully regenerable with standard equipment

• The catalyst needs to keep at least the same• Chloride retention• Mechanical properties

• Surface area stability needs to be improved to• Extend catalyst life• Ensure higher chloride retention throughout entire service life• Reduce production of fines

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Chemistry Optimization

New Promoters developed to

1. Increase catalyst selectivity by minimizing the cracking reactions & ring opening

Higher H2 & C5+ yields

2. Increase catalyst stability by minimizing coke deposit on the catalystAllow to operate at lower recycle gas ratios

Yields increaseReduction of utility consumption

3. As topping on the cake - the Pt content has been reduced while catalyst stability has increased

Lower cost

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Today: 40 units in operation

Axens Licensed Units in Operation

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Criterion Legacy & Axens CCR Catalyst in Non Axens Units

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Criterion legacy & Axens CCR Catalyst in Non Axens Units

Axens design ; Non Axens design

Almost 100 units in Operation

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Axens CCR Reforming Catalyst Portfolio

Application Gasoline Aros Gasoline / Aromatics

Pt, wt% 0.25 0.30 0.29 0.29

Promoters Sn + Others (Multi-Promoted)

Moving bed density, t/m3 0.65 0.65 0.54 0.54

Main Attributes Yields Strength

Activity Strength

Activity Strength

Activity Yields

Strength

Target Unit All All Competitor

CR 600’s AR 700’s PS 100

Standard DensityHigh Density

PS 40

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PS-40: Top performer for over 10 years! Set the Standard for Performance Excellence.

C5+ yield: 1.0 -1.3 vol% more,

H2 Yield: 0.15 - 0.2 wt% more,

Feed Thru-put: 15 -30% more

Coke Lay-down: 20–30% less,

Cl Consumption: 10-30% less,

Make Up Catalyst: 50-60% less

CCR Reforming Standard Density Catalyst

More than 40 Non-Axens Design Units Supplied Worldwide

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CCR Reforming Standard Density Catalyst

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Evidence of Higher Surface Area Retention

Axens’

CR 600 & AR 700 provide the best surface area retention

120

140

160

180

200

220

0 100 200 300 400TOS [h]

Spec

ific

surfa

ce a

rea

[m2/

g]

Sample A CR 607

CR 600

20 m2/g

Pt/Sn

Surface loss•

Pt/Sn •

∆Surface = 55 m²/g

CR 607•

∆Surface = 22 m²/g

Operating conditions : Mixture of N2

& H2

O•

20% vol. water, at 650°C

Hydrothermal stability has beenimproved by a factor 2

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Summary of Improvements New Generation Catalysts

• Better yields• Hydrogen + 0.1 wt%• Reformate + 1 wt%

• Coke make decreased by +30 %

• Fully regenerable with standard regenerator

• Surface area stability improved by a factor 2

• Lower platinum content

Targets are achieved

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New Developments Standard Density Catalyst

•The result from the combination of Axens & Criterion’s catalytic Reforming technology. Leaders in catalytic formulations andsuperior Alumina Support Technology.

• Ultimate Selectivity.

• Improved Activity for units with no pinninglimitations.

•Same Physical Characteristics as PS-40:•Lower Attrition Rates•Lower Fines make•Surface Area Retention•Chloride Retention

Available in 2012!PS 100New

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CCR Reforming High Density Catalyst

• Reasons to justify High Density Catalysts

• Activity constraints• Fire Heater limitations

• High skin temperatures• High WAIT

• Pinning constraints

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Summary

• Axens & Criterion Reforming business have merged

• The PR & PS Catalyst are still available

• New products are coming out soon

• R&D is working to take all the benefit of the two corporation knowledge

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Thank You for your attention

Visit us at : http://www.axens.net