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FACS - 31/3/2014 Global Refining Summit 2014

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This presentation was held 31 March of 2014 at the Global Refining Summit in Barcelona. It is about addressing four technical challenges to survive in the era of increased energy costs, depreciating profit margins, debilitating regulations, environmental restrictions and declining crude quality.

TRANSCRIPT

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FACS - 31/3/2014Global Refining Summit 2014

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Dynamic Heat Exchange SolutionsSignificant cost saving for refineries by innovative process

equipment

Femke Schaëfer

Barcelona – March 31st , 2014

Global Refining Summit 2014 FACS - 31/3/2014

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Topics:

• Short introduction to Bronswerk Heat Transfer®

• Improvement areas in refinery

• Three case studies

• Bonus

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Introduction

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Our markets:

Sustainability Service & Maintenance

Power

Oil

Gas

Chemical

Air Handling

Food Processing

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What we do:

• Thermal designs:

based on:

Aspen/HTFS

HTRI

HEI

Computational Fluid Dynamics

Hysys

Global Refining Summit 2014 FACS - 31/3/2014

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What we do:

• Mechanical designs:

- ASME

- EN13445

- AD2000

- RTOD

- PD5500

- CODAP

- GOST

FEM analysis

Global Refining Summit 2014 FACS - 31/3/2014

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What we do :

• Process design:

Process optimization

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What we do :

• Equipment:

Heat exchangers

Air cooled coolers

And other process

equipment

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What we do :

• Materials:

Titanium

(Super)Duplex

Nickel-Alloy

Inconel

Other exotics

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What we do :

• Systems:

Incl. controls

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What we do :

• Site work: Erection Assembly Start up Commissioning Service

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What we do :

• Service & Maintenance: Upgrading Debottlenecking Inspection Specialist

maintenance for machines operating hazardous materials

Global Refining Summit 2014 FACS - 31/3/2014

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Our focus on innovation:

• Product development

• System solutions

• New technology

Compact Header®

Radiax®

Whizz-Wheel® fans

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Area’s for improvement

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One: Newbuilds or Upgrading

Start at the source: size reduction of process equipment during design

Size of S&T heat exchangers

Nr of S&T heat exchangers

Size of air cooled coolers

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Two: Improvement of installation

During operation; more efficient power consumption

25-30% of worlds energy

consumption is used for

ventilation

Increasing output

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Three: Less downtime

Maintenance; limitation of production losses by fouling reduction in

Heat Exchangers

Crude oil quality is dropping

Decreasing production output

Higher energy use and CO2

emission

Maintenance is costly

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The solutions

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Current situation:

•Huge plot space requirement

•High power consumption for air coolers

•Big influence on CAPEX & OPEX

Case study 1 – High efficiency cooling

Global Refining Summit 2014 FACS - 31/3/2014

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Case study 1 – High efficiency cooling

•New fan design based on

aerospace technology

•Intensified heat transfer

through higher air

pressure and velocity

•Over 30% plot space

reduction

OR

•Over 50% reduction in

power consumption

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Original design based on standard air coolers;

• Absorbed electrical power: 1143 kW

• Plot space used: 4224 m²

• Noise power emission: 101 dB(A)

Case study 1 – High efficiency cooling

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Improved design based on high efficiency air coolers (with Whizz-Wheel® fans);

Old New

• Absorbed electrical power: 1143 kW 528 kW

• Plot space used: 4224m² 2974 m²

• Noise power emission: 101 dB(A) 94 dB(A)

Case study 1 – High efficieny cooling

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Benefits;

• Noise reduction: 7 dB(A)

• Size reduction: 1250 m² = 29%

• Power consump. red.: 615 kW = 53%

• Opex savings: € 492.000,- / yr Figure 3: comparative

Figure 2: high efficiency designFigure 1: standard design

Case study 1 – High efficiency cooling

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VS

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Increasing output

• 50% less kW

• 35% more cooling air

• 10-15% more production

• € 700 million gas production

• € 70 million additional

• Debottlenecking investment: € 0,5 million

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Increasing output

Restrictions:

• Maximum noise level

• Production capacity

down to 60%

Results:

• Elimination of all

noise issues

• Production up to

100%

Bonus:

• 56% savings in

energy consumption

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Increasing output

Restrictions:

• Lower noise level or

plant shut down!

Results:

• 20 fans installed

• Elimination of all

noise issues

Bonus:

• 56% savings in

energy consumption

Global Refining Summit 2014 FACS - 31/3/2014

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High pressure compact cooling & maintenance

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Case study 2 – High pressure compact cooling

Situation: Conventional high pressure S&T HEX at a refinery

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Original design based on conventional D-type high pressure shell & tube heat

exchangers;

Global Refining Summit 2014 FACS - 31/3/2014

• Design pressure 450 bar

tubeside

• Design pressure 350 bar

shell side

Case study 2 – High pressure compact cooling

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New design based on compact header® high pressure shell & tube heat

exchangers;

Global Refining Summit 2014 FACS - 31/3/2014

• Design pressure 450 bar

tubeside

• Design pressure 350 bar

shell side

Case study 2 – High pressure compact cooling

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• Up to 60% weight reduction

• Reduced plot space

• Much higher allowable

temperature gradients

• High pressure is no issue up to

1000 bar

• Easy maintenance

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Case study 2 – High pressure compact cooling

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Plugs

Maintenance

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Fouling prevention

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Case study 3 – Fouling prevention

Situation: Fouling inside thermosyphon reboiler tubes in crude stabilization unit in

Abqaiq

Source: http://www.ortloff.com/sulfur-recovery/modified-claus-process-with-tailgas-cleanup/

Global Refining Summit 2014 FACS - 31/3/2014

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Original design based on thermosyphon reboiler;

Case study 3 – Fouling prevention

Shell side: steam

• Inlet temp: 157°C

• Outlet temp: 87°C

Tube side: Crude oil (Arabian light)

•Inlet temp: 70°C

•Outlet temp: 85°C

Heat transfer surface: 6000m2

Maintenance:

•Cleaning of tubes: 1-2 months

•Retubing: 2 years

Source: http://upload.wikimedia.org/wikipedia/commons/5/57/Thermosyphon_Reboiler.png

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Case study 3 – Fouling prevention

Alternative design based on Klarex® shell & tube heat exchangers;

Global Refining Summit 2014 FACS - 31/3/2014

Original Alternative

Shell side fluid: steam

• Inlet temp: 157°C

• Outlet temp: 87°C

Tube side: Crude oil (Arabian light)

•Inlet temp: 70°C

•Outlet temp: 85°C

Heat transfer surface: 6000m2 4600m2

Maintenance:

•Cleaning of tubes: 1-2 months 2-3 years

•Retubing: 2 years 2 years

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• Fluidized (vertically entrained)

cleaning particles inside the tubes

• This prevents deposition of wall-

fouling compounds (turbulence)

• Heat transfer enhancement due to

change from laminar flow pattern

into turbulent flow

• Smaller heat transfer surface

required

• Continuous operation

Case study 3 – Fouling prevention

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Case study 3 – Fouling prevention

Global Refining Summit 2014

Benefits:

• Heat transfer surface reduction: 1.400 m2 = 34%

• Saving in Opex:

• Maintenance = € 84.000,- x 40 (reboiler) = € 3.4 million/yr

• Capex: For new plant - 1 klarex instead of 2 reboilers

• 1 reboiler € 850.000,- x 40 reboilers = € 34 million

• 1 klarex € 950.000,- x 20 klarex heat exchangers = € 19 million

15 million less Capex and 3.4 million less Opex every year.

FACS - 31/3/2014

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Situation: Shell side fouling conventional naphta exchanger in the recovery

process in Abqaiq

Global Refining Summit 2014 FACS - 31/3/2014

Case study 3 – Fouling prevention

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Case study 3 – Fouling prevention

Original design based on conventional naphta exchanger;

Parameters naphta exchanger:

• Tube side: lean oil

• Shell side: rich oil

Maintenance:

•Cleaning: every 2-3 months

•Retubing: every year

•Costs: € 30.000,-

•Total costs in 1 years: € 165.000,-

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Case study 3 – Fouling prevention

Alternative design based on Twist-Flex-Baffle ® exchanger;

Parameters Twist-Flex-Baffle® exchanger:

• Tube side: lean oil

• Shell side: rich oil

Maintenance:

•Cleaning: every 2 years

•Retubing: every year

Benefits:

•Improved heat transfer: > 10%

•Reduced pressure loss: > 10%

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Flare gas recoveryFlare gas compression with smart-compact Radiax ®compressor:

• Several hundreds of millions m3 of flare gas wasted

• Gas at atmospheric pressure

• Compress to 20-80 Bar

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Flare gas recoveryFlare gas compression with smart-compact Radiax ®compressor:

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Flare gas recoveryFlare gas compression with smart-compact Radiax ®compressor:

• Several hundreds of millions of flare gas wasted

• Gas at atmospheric pressure

• Compress to 20-80 Bar

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Summary

Yes, Bronswerk Heat Transfer can help your refinery become more sustainable and profitable at the same time:

1. Start at the source: size reduction of process equipment during design

Global Refining Summit 2014 FACS - 31/3/2014

Klarex® 34% in heat transfer surface

Twist-Flex-Baffle® 10% improved heat transfer

High efficiency air coolers with

Whizz-Wheels®

up to 30% in plot space area

Flexplate® additional 25-30% in plot space

Radiax® Compressor/Turbine up to 95% in space requirement

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Summary

2. During operation; reduction of power consumption

Global Refining Summit 2014 FACS - 31/3/2014

High efficiency air coolers with

Whizz-wheels®

Power consumption reduction up

to 50%

Radiax® Compressor/Turbine Energy recovery: € 7,5 mill a year

Without additional investment

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Summary

3. Maintenance; limitation of production losses by fouling reduction in Heat Exchangers

Global Refining Summit 2014 FACS - 31/3/2014

Klarex® OPEX savings of € 3,4 million a year

Twist-Flex-Baffle® OPEX savings of € 165.000,-

a year

Compact Header® HEX Easy one-man-maintenance

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Thank you for your attention.Questions please

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How to contact us:

www.bronswerk.com

facebook.com/bronswerk

Linkedin.com/company/bronswerk-heat-transfer

twitter.com/bronswerk

Global Refining Summit 2014 FACS - 31/3/2014

And come visit our booth in the central hall