kbr, mahesh gandhi

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Page 1: KBR, Mahesh Gandhi
Page 2: KBR, Mahesh Gandhi

Technical innovations improving the sustainability and efficiency of the fertilizer industry

Mahesh Gandhi (MG)

Boost Ammonia Conversion Using KBR Ammonia Revamp Technologies Kellogg Brown & Root LLC

Organization logo to appear here

2 ©2015 KBR, Inc. All Rights Reserved 2

Page 3: KBR, Mahesh Gandhi

• Safety Moment

• Overview - Why Retrofit?

• Current KBR Synthesis Loop Technology

• Impact of Increased Ammonia Concentration

• Converter Retrofit Options – Add-on Converter verses In-situ

– Cold Wall – the only choice

• Add-on Converter Options – With inter-changer & Without Inter-changer

• Conclusion

Organization logo to appear here

Boost Ammonia Conversion Using KBR Ammonia Revamp Technologies

3

Page 4: KBR, Mahesh Gandhi

SAFETY MOMENT

4

YOU ARE RESPONSIBLE FOR YOUR SAFETY!

SAFETY STARTS WITH YOU – YOU CREATE A CULTURE OF

SAFETY

ZERO ACCIDENT MEANS EVERY ONE RETURNS HOME

IN THE CONDITION THEY CAME TO WORK!

Page 5: KBR, Mahesh Gandhi

Overview - Why Retrofit?

Simple Answer is Economics – lower per unit production cost

Most producers consider retrofit first before a new plant

Retrofitting also offers following additional advantages:

No increase in plot space or operating personnel

Not much additional operational training required

Not much change in the maintenance procedures

Minimum OSBL changes

5

Page 6: KBR, Mahesh Gandhi

Vintage Ammonia Plants Need to Compete

• Increased Capacity

• Reduced Energy Consumption

• Reduced Natural Gas Usage

• Higher On-stream Factor

Low Cost Ammonia Production

•Well Integrated Proven Process

• Sustained Life-Cycle Benefit

•Guarantees to Support Viability

Successful Revamp Project &

Operations

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Page 7: KBR, Mahesh Gandhi

Ammonia Plant Revamp Technology

Ammonia Revamp

Process Flow-sheet

Existing Equipment

New Equipment

KBR Proprietary Equipment

Modified Equipment

• Implement as Integrated Whole Plant Flow-sheet

• Even One Bottleneck Missed in Scoping, Leads to Missed Capacity & Energy Targets

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Page 8: KBR, Mahesh Gandhi

Sections in an Ammonia Plant

Reforming Syngas

Purification Synthesis

Loop

Natural

Gas

Process Air CO2

NH3

Steam & Water System

Condensate

Steam

Make-up Water

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Page 9: KBR, Mahesh Gandhi

Ammonia Synthesis Loop - Typical

Syngas

HP Steam

CW

Synloop Purge

0 C

Syngas

Compressor

BFW

Ammonia Product

Converter System

Chilling System

Refrigeration

Compressor

Use dry make-up syngas or remove moisture by passing through ammonia chillers in loop

Hot side of the loop has converter, heat recovery to steam system & exchanger

Cold side has CW cooler, chilling, separator and purge

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Page 10: KBR, Mahesh Gandhi

CURRENT KBR SYNTHESIS LOOP

Syngas

CW

0 C

Refrigeration

Compressor

Horizontal Converter

Unitized

Chiller

BFW

NH3 Prod

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Page 11: KBR, Mahesh Gandhi

1 2 3-A 3-B

FEEDEFFLUENT

BYPASS OR

FROM 102-B

Horizontal converter with Three equilibrium stages with two

intercoolers.

Removable catalyst basket within the pressure shell.

An annular space exists between the cylindrical catalyst basket and

the high pressure shell to provide a path for feed gas cooling the

shell.

The process flow is downwards through each bed. Low pressure

drop. All of the feed gas passes through each of the catalyst beds.

Four beds, each filled with promoted iron catalyst of 1.5 - 3 mm at

top 90% and 3-6 mm granules bottom 10%.

1 2 3-A 3-B

FEEDEFFLUENT

BYPASS OR

FROM 102-B

11

Ammonia Converter (105-D)

Page 12: KBR, Mahesh Gandhi

Ammonia Synthesis Loop- More Types

Syngas

BFW

HP Steam

Recycle

To Cooling & Chilling

First Converter

Second Converter

Syngas Compressor

Some synthesis loops have separate converters with external heat exchangers

Location of make-up gas addition to loop varies

Wet loops require a separate delivery of make-up syngas from compressor to chilling section

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Page 13: KBR, Mahesh Gandhi

Ammonia Converter Systems - Typical

Vintage converter systems are 3 adiabatic bed intercooled designs

Older vintage have 2 adiabatic bed intercooled designs

Vertical as well as horizontal converters in use

Converters with combined beds & intercoolers may typically have COLD WALL pressure vessel operating below ~250C

A separate converter to boost conversion after heat recovery requires HOT WALL vessel in grass-root or revamp project

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Page 14: KBR, Mahesh Gandhi

KBR Magnetite Ammonia Converters

Vertical converters

1960s to mid 80’s

(total ~150)

Initial vertical “Slim

Jim” with separate cold

product sweep gas

Two adiabatic bed

horizontal since 80’

Three adiabatic bed

horizontal since 90’

Vintage Braun

separate vertical

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Page 15: KBR, Mahesh Gandhi

Boosting conversion in ammonia synloop improves economics

Higher conversion provides more capacity & energy saving

More ammonia condensed in CW cooler, less duty on refrigeration

Less power for syngas & refrigeration machines saves fuel energy

Boosting Ammonia Conversion Helps…

Isothermal/MRR Adiabatic

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Page 16: KBR, Mahesh Gandhi

Disadvantages of Hot Wall Ammonia Converters

With given hot feed gas, vessel is exposed to high

temperatures in aggressive H2/N2 environment

High Cr-Mo hot wall vessel is thick, requires rigorous shop QC,

fewer vendors, expensive, low reliability

Hot wall converters seen to experience weld cracking over

period, cold wall have long life

Hot wall desired to have controlled pressurization/

depressurization & cooling/heating production loss

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Page 17: KBR, Mahesh Gandhi

Add Converter in Series to Boost Conversion

Adiabatic converter in series provides cost effective increase

in capacity & energy saving

Challenge is- the second converter must be hot wall design

due to hot feed gas

Add on converter typically has high risk & cost, due to

mandatory “hot wall”

KBR True Cold Wall Add On option provides risk mitigation &

low cost project

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Page 18: KBR, Mahesh Gandhi

Ammonia converter added in series to

boost conversion

Proven vintage MWK design, cold gas

sweep, like “Slim-Jim” of 1960’s

Cold wall 150+ still in use, 30-50 yrs

Patented annulus flow feature

KBR’s True Cold Wall Add-on Converter

Cooling

Gas

Feed

Product

Cooling

Gas

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Page 19: KBR, Mahesh Gandhi

Cold sweep gas stream passes through annular space, no mixing with reacting gas

Cold sweep stream taken from cold part of the synloop

Revamp for capacity gain, energy saving or reliability

Can also replace existing unreliable hot wall converters

Low cost, multiple vendors

KBR’s True Cold Wall Add-on Converter

Cooling

Gas

Feed

Product

Cooling

Gas

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Page 20: KBR, Mahesh Gandhi

Thin screen and profiled wire internals in existing converters nitride over years

Internals need replaced, typically done while replacing catalyst

KBR offers proven, 3 adiabatic bed, replacement basket for horizontal converter

KBR also offers 3 adiabatic bed, intercooled, in situ replacement basket for vertical MWK/KBR converters

We provide material and field services

KBR’s High Conversion Replacement

Baskets

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Page 21: KBR, Mahesh Gandhi

Boosting ammonia conversion in existing synthesis loop provides increased capacity and saves energy

Others require hot wall vessel, KBR’s True Cold Wall Add-on Converter provides reliable, low cost, effective revamp solution

Proven features of “Slim Jim” used

KBR also provides insitu replacement baskets for vertical and horizontal converters to boost conversion

Conclusion

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Page 22: KBR, Mahesh Gandhi

22 ©2015 KBR, Inc. All Rights Reserved