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02 EPC PET vantage revamping

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► plant conversion for alternative raw materials, or production of new polymers specialities application in fibres/ filament yarns PETvantage® Revamping Conceptions Market Driven Approac

Trang 1

EPC PETvantage - Plant Modernization

Revamp | Capacity increase

ENGINEERING & PLANT CONSTRUCTION

®

The EPC Group is certified according to DIN EN ISO 9001:2008

Trang 2

► plant conversion for alternative raw materials, or

production of new polymers

specialities application

in fibres/ filament yarns

PETvantage® Revamping Conceptions

Market Driven Approach - Strategic Revamping

Trang 3

► Systematic Business Process (1/4)

Technical Feasibility Study

Market Driven Approach - Strategic Analysis

Trang 4

► Systematic Business Process (2/4)

Technical Feasibility Study

Market Driven Approach - Strategic Analysis

Trang 5

► Systematic Business Process (3/4)

Investment Pay-Off Estimate - All Scenarios (DYNAMIC)

IndustrialEngineering ALL COST in US-Dollar, based on an USD/EUR exchange rate of: 1,260 on November 20, 2008 0,800

2,230 0,900 130

Fix cost USD/MT 43,7 58,5 35,3 58,5 35,3 54,8 35,3 53,1 39,0 36,4 21,3 36,4 19,4 36,4 19,4

Annual fix cost USD 1.986.120 2.250.943 1.851.113 2.250.943 1.851.113 2.108.836 1.851.113 2.043.151 2.043.151 1.909.699 2.187.179 1.909.699 1.995.141 1.909.699 1.995.141

1.307 1.299 991 1.299 991 1.002 991 976 976 991 976 991 976 991 976

130.499.359 1.065

IPA price in USD/kg:

MEG price in USD/kg:

SENSITIVITY ANALYSIS PTA price in USD/kg:

Gross profit margin in USD:

Additional profit margin on add capacity in USD

Total annual production cost (@350 days/year) in USD 123.235.032

Total average production cost

in USD/MT 1.467

25.809.666 26.819.502 14.378.073

114.461.874 1.258

3.486.297 3.955.991

Yearly fix cost savings in USD corresponding to production rate development 135.007 342.799

140.000

Yearly variable production cost savings in USD 1.437.455

Yearly raw material cost savings in USD based on max 150 MT/D capacity

SCENARIO 3A2

116.842

1.066 4.511.972

26.819.502 140.186

5.082.814 1.084

167.926.652 99.317.275

100.442

277.114 284.214

5.285.930

11.002.163 10.651.325

332.224 26.819.502

2.180.622 26.819.502

113.769.586 168.672.644 1.109 1.091 1.071 100.878.890

Technical Feasibility Study

Market Driven Approach - Strategic Analysis

Trang 6

► Systematic Business Process (3/4)

Investment Pay-Off Estimate - All Scenarios (DYNAMIC)

2,230 0,900 130

CPU-DMT BPU-DMT CPU-PTA BPU-DMT CPU-PTA BPU-PTA CPU-PTA CBPU CPU-PTA CBPU CPU-PTA CBPU CPU-PTA CBPU CPU-PTA TEX BGC TEX BGC TEX BGC TEX BGC BGC TEX BGC TEX BGC TEX BGC

MT/D 130 110 150 110 150 110 150 110 150 150 300 150 300 150 350

IPA price in USD/kg:

MEG price in USD/kg:

SENSITIVITY ANALYSIS

PTA price in USD/kg:

Gross profit margin in USD:

SCENARIO 3A2 SCENARIO 3A1

SCENARIO 2 SCENARIO 2A SCENARIO 3 SCENARIO DMT SCENARIO 1

BGC = bottle grade chips, TEX = textile grade polymer

Technical Feasibility Study

Market Driven Approach - Strategic Analysis

Trang 7

Market Driven Approach - Strategic Business Design

A Technological Feasibility Study defined the appropriate design

…resulting in a business-technological “best-case”conception:

during Implementation of Revamping Scope

Trang 8

► tailor-made process plant re-design

► no change of existing reactors

The continuous Polycondensation Capacity Lift

EPC VARIPLANT®

Technology for a successful business future:

Market Driven Approach - PETvantage

Trang 9

► Polycondensation Capacity Lift is “Must”

Capacity Lift Needs

Trang 10

Utilities/

Energy requirements

Market Driven Approach - PETvantage

Trang 11

PET plant capacity lift potentials

Polycondensation Capacity Lift is “Must” to stay competitive through

“Economics-of-Scale”, especially if you take into account that new

production plants with capacities above 1200 t/d will be online in the near future

Before Revamping After Revamping

Trang 12

Examples of Significant Achievements Market Driven Approach - PETvantage

Trang 13

PET Plant Capacity Lift and Upgrade / Modernisation

Location Volos / Greece

Services of EPC • Feasibility Study

Trang 14

► Capacity-, Reliability- & Production Quality Increase

by Modification of a Finisher - … and something more

A very special version of “capacity lift”!

PET Plant Capacity Lift and Upgrade / Modernisation

Trang 15

PET Plant Capacity Lift and Upgrade / Modernisation

Location Bobingen / Germany

Services of EPC • Feasibility Study

Trang 16

► Capacity Lift and Polymer Specialities Production

PET Plant Capacity Lift and Upgrade / Modernisation

Trang 17

Conversion of 4 Existing PET Polycondensation Lines

For PET-chips production from textile fibers to food grade PET-chips (bottle –PET) with simultaneous capacity increase to 1.000 tons per day

Location Yanbu / Saudi Arabia

Services of EPC

• Feasibility Study

• Technological Design

• General Engineering

• Functional Turn-Key Contractor

• Functional Turn-Key, Erection Supervision

• Commissioning Supervision

Client IBN Rushd Saudi Arabia

(a SABIC affiliate)

Realization 2006 - 2009

Trang 18

► World-Largest PET Plant Conversion & Debottlenecking

Market Driven Approach - PETvantage

Trang 19

► World-Largest PET Plant Conversion & Debottlenecking

Market Driven Approach - PETvantage

Trang 20

► World-Largest PET Plant Conversion & Debottlenecking

Market Driven Approach - PETvantage

Trang 21

► World-Largest PET Plant Conversion & Debottlenecking

Market Driven Approach - PETvantage

Trang 22

Market Driven Approach - PETvantage

350’000 tons/a PET capacity reached

Trang 23

► World-Largest PET Plant Conversion & Debottlenecking

per 1 ton of PET, e.g.:

Market Driven Approach - PETvantage

Trang 24

► World-Largest PET Plant Conversion & Debottlenecking

some key parameter like:

☺ Acetaldehyde content in BG chips: < 0.3 ppm

☺ Thermal Stress on polymer melt,

Market Driven Approach - PETvantage

Trang 25

EPC InsidePET® - Advanced Plant Process Control

Market Driven Approach - PETvantage

Trang 26

EPC InsidePET

EXAMPLE (1/3):

Esterification reaction progress control by reactive surface renewal

Automated parameter setting corresponding to plant throughput , including reactive molar ratios correction

COOH end groups setting

for a consistent carboxylic end group level in PET

-COOH end groups control

due to high PTA particle size fluctuation

Reactive molar ratio control

including process glycol components determination confidential

confidential

confidential

confidential confidential confidential

confidential

confidential confidential confidential confidential

confidential

Market Driven Approach - PETvantage

Trang 27

Let’s move forward together!

EPC Engineering Consulting GmbH

Mr Karol Kerrane Business Development Manager Contact

Breitscheidstraße 152

07407 Rudolstadt Germany

Phone: +49 3672 302 300 Email: karol.kerrane@epc.com

www.epc.com

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