Non- -electrical Application electrical Application Non of - - PowerPoint PPT Presentation

non electrical application electrical application non of
SMART_READER_LITE
LIVE PREVIEW

Non- -electrical Application electrical Application Non of - - PowerPoint PPT Presentation

Non- -electrical Application electrical Application Non of nuclear Power of nuclear Power Desalination and Water Reuse Desalination and Water Reuse- - A technology for the future A technology for the future Ghassan Ejjeh-


slide-1
SLIDE 1

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Non Non-

  • electrical Application

electrical Application

  • f nuclear Power
  • f nuclear Power

“ “Desalination and Water Reuse Desalination and Water Reuse-

  • A technology for the future

A technology for the future”

Ghassan Ejjeh Ghassan Ejjeh-

  • Director

Director IDA and Six Construct IDA and Six Construct Leon Awerbuch Leon Awerbuch-

  • President LET, Director IDA

President LET, Director IDA 17 April 2007, 17 April 2007, Oarai Oarai

slide-2
SLIDE 2

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

World Water World Water World Water

Salt Water Salt Water 97.5% 97.5% Total Fresh Water 2.5% Total Fresh Water 2.5%

68.9% Glaciers and permanent snow cover 68.9% Glaciers and permanent snow cover 29.9% Fresh Groundwater 29.9% Fresh Groundwater 0.3% renewable 0.3% renewable Freshwater Freshwater 0.9% Other 0.9% Other (swamps, moisture, etc.) (swamps, moisture, etc.)

slide-3
SLIDE 3

I ncreased Water Demands: I ncreased Water Demands:

Greater extraction of groundwater Greater extraction of groundwater resulting in depletion of the aquifers, resulting in depletion of the aquifers, The only available choice, to meet the The only available choice, to meet the demand demand is is

SEA WATER DESALI NATI ON SEA WATER DESALI NATI ON

slide-4
SLIDE 4

Desalination will create Desalination will create sustainable sustainable development of extra water resources development of extra water resources Help minimize regional and international Help minimize regional and international conflicts, over sharing of water. conflicts, over sharing of water. Will offer commercial opportunity of Will offer commercial opportunity of 80 80 billion dollars plus, in the next 10 billion dollars plus, in the next 10-

  • 20 years.

20 years.

slide-5
SLIDE 5

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

The Challenge The Challenge

  • The need for ever increasing quantities of low cost

desalinated water

  • To ensure environmentally sustainable expansion

in supply

  • To create a product which is reliable and can

attract finance

slide-6
SLIDE 6

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

MARKET DRIVERS for MARKET DRIVERS for DESALINATION and POWER DESALINATION and POWER

  • Increasing water demand
  • Decreasing unit cost of desalination through technology

improvement

  • Lack of alternatives to desalination
  • Environmental constraints increasing the cost of traditional

water resources

  • Imbalance between rapid growth of water demand and

slower growth of peak power

  • Water can be stored, whereas electricity cannot
slide-7
SLIDE 7

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

TRENDS IN DESALINATION AND TRENDS IN DESALINATION AND POWER MARKETS POWER MARKETS

  • Movement towards market pricing of water
  • Privatisation of water supply
  • Introduction of Build Own and Operated

(BOO) concept to power and desalination projects

  • Profitability moving from manufacturing to
  • wnership and O&M
  • Hybrid and Nanofiltration (NF) as a

solution to the power surplus and need for cost reduction.

slide-8
SLIDE 8

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Desalting Inventory Desalting Inventory

Worldwide there are 15,233 desalting units with total capacity of 32,400,000 m3 /d or 5,706 MIGPD

  • Over the last two years the increase averaged

10.5% / year

  • The Middle East is still the dominant market

Saudi Arabia 22.4% UAE 20.4% USA 12.0% Kuwait 8.4%

slide-9
SLIDE 9

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Australia 0.8% Caribbean 3.5% Europe 13.3% Middle East 49.1% Asia 11.2% Africa 5.1% North America 16.2% South America 0.8%

By Region

Total desalination capacity worldwide

slide-10
SLIDE 10

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Total desalination capacity Total desalination capacity worldwide by the source water. worldwide by the source water.

By Capacity Seawater Brackish water River water Pure water Brine Waste- water

slide-11
SLIDE 11

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Desalting Inventory Technology Desalting Inventory Technology

For all plants installed and contracted

  • MSF represents 43.5%
  • RO represents 43.5%

For seawater as a feed

  • MSF represents 66.3%
  • RO represents 22.4%
  • MED and HYBRIDS coming strong
slide-12
SLIDE 12

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

The significant increase in fuel-energy and material cost has a dramatic impact on capital and operational cost of Desalination and Power plants. Impact of US$ 60-75 per barrel oil, natural gas exceeding 11 $/MMBTU and high demand for raw materials, steel, copper, nickel and concrete has dramatically increased pressure to develop novel solutions. Can we minimize energy consumption and reduce volume and weight of desalination plants?

slide-13
SLIDE 13

Desalination is an energy and capital Desalination is an energy and capital intensive process. intensive process. All major desalination technologies Multistage All major desalination technologies Multistage Flash (MSF), Multi Flash (MSF), Multi-

  • effect Distillation (MED and

effect Distillation (MED and MED TVC), and Mechanical Vapor Compression MED TVC), and Mechanical Vapor Compression (MVC) as well as Reverse Osmosis (RO) and (MVC) as well as Reverse Osmosis (RO) and Hybrids will be significantly affected by Hybrids will be significantly affected by energy costs energy costs

slide-14
SLIDE 14

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Energy Requirements Energy Requirements (Steam/Electricity) (Steam/Electricity)

Process Live Steam Process Live Steam Electricity Electricity (ton product/ ton steam) (ton product/ ton steam) kwh/ ton kwh/ ton product product

Multi Stage Flash Multi Stage Flash 8 8 4 4 Vapour Compression Vapour Compression n/a n/a 8 8 Multi Effect Distillation Multi Effect Distillation 12 12 2 2 Reverse Osmosis: Reverse Osmosis: with energy recovery with energy recovery n/a n/a 3.5 3.5-

  • 5.5

5.5 without energy recovery without energy recovery n/a n/a 8.5 8.5

slide-15
SLIDE 15

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Desalination Technologies Desalination Technologies

  • Multi

Multi-

  • Stage

Stage-

  • Flash

Flash Distillation (MSF) Distillation (MSF)

  • Multi

Multi-

  • Effect

Effect-

  • Distillation (MED)

Distillation (MED)

  • Reverse Osmosis

Reverse Osmosis (RO) (RO)

  • Vapour Compression

Vapour Compression Distillation (VCD) Distillation (VCD)

slide-16
SLIDE 16

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Thermally driven Desalination Thermally driven Desalination Technologies Technologies

  • Multi

Multi-

  • stage Flash (MSF)

stage Flash (MSF)

  • Multi

Multi-

  • effect Distillation (MED)

effect Distillation (MED)

  • Multi

Multi-

  • effect Distillation with

effect Distillation with Thermocompression (MED Thermocompression (MED -

  • TC)

TC)

slide-17
SLIDE 17

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Multi Stage Flash (MSF) Multi Stage Flash (MSF)

  • Raw seawater total dissolved solids (TDS):

Raw seawater total dissolved solids (TDS): 35 35-

  • 47,000 mg/L

47,000 mg/L

  • Maximum brine temperature: 112

Maximum brine temperature: 112o

  • C

C

  • Performance ratio: 8

Performance ratio: 8

  • Electrical power: 3

Electrical power: 3-

  • 4 kWh/m

4 kWh/m3

3

  • Scale inhibitors used for scale control

Scale inhibitors used for scale control

  • Recycle type plant

Recycle type plant

  • Dual purpose plant

Dual purpose plant

slide-18
SLIDE 18

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

  • MSF well established reliable technology with the limits

MSF well established reliable technology with the limits for Performance Ratio (PR) of PR= 10 typical PR= 8, for Performance Ratio (PR) of PR= 10 typical PR= 8, internal power consumption of 4kWhr/ton of water, internal power consumption of 4kWhr/ton of water, with turndown ratio from 110 with turndown ratio from 110-

  • 70% of nominal

70% of nominal capacity capital cost $4.00 capacity capital cost $4.00-

  • $8.00 per gallon per day

$8.00 per gallon per day installed (GPD). installed (GPD).

slide-19
SLIDE 19

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

slide-20
SLIDE 20

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

MSF KEY PARAMETERS MSF KEY PARAMETERS

Capital Cost MSF 5.5 US$ MM per MIGD Capital Cost –Intake /Outfall 0.1 US$ MM per MIGD

  • f cooling

MSF GOR 8 Tons of product/ton

  • f steam

LP Steam Supply 2.5-3

  • Bar. A

Lost Power Potential 1.225 MW/MIGD Power Consumption 4 kW.hr/m³ of distillate Steam Consumption 23.7 Tons/MIGD Chemical Costs 40,000 US$/yr per MIGD MSF R&R 1% TIC/yr Labor 40,000 US$/yr per MIGD

slide-21
SLIDE 21

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Multi Effect Distillation (MED) Multi Effect Distillation (MED)

  • Raw seawater total dissolved solids

Raw seawater total dissolved solids (TDS): 35 (TDS): 35-

  • 47,000 mg/L

47,000 mg/L

  • Maximum brine temperature: 76

Maximum brine temperature: 76o

  • C

C

  • Performance ratio: 12

Performance ratio: 12

  • Electrical power: 2 kWh/m

Electrical power: 2 kWh/m3

3

  • Scale inhibitors used for scale control

Scale inhibitors used for scale control

  • Dual purpose plant

Dual purpose plant

slide-22
SLIDE 22

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

  • MED with wide range of performance ratios from PR

MED with wide range of performance ratios from PR-

  • 8

8 to PR to PR-

  • 16, typical PR= 12, internal power consumption

16, typical PR= 12, internal power consumption

  • f 1.8
  • f 1.8 kWhr

kWhr/ton of water with turndown ratios from /ton of water with turndown ratios from 120 to 45% of nominal capacity, capital cost of MED 120 to 45% of nominal capacity, capital cost of MED plants vary from $3.50 plants vary from $3.50-

  • $7.00 per GPD.

$7.00 per GPD. MED unit Thermocompression (MED MED unit Thermocompression (MED-

  • TC) are similar in

TC) are similar in characteristic to MED but require higher pressure characteristic to MED but require higher pressure steam steam-

  • jet compressor acting as the heat pump. They

jet compressor acting as the heat pump. They are designed where 2 to 10 atm steam is available, for are designed where 2 to 10 atm steam is available, for water vapour to be thermocompressed across several water vapour to be thermocompressed across several

  • effects. MED
  • effects. MED-
  • TC is particularly in use with Gas

TC is particularly in use with Gas Turbines. Turbines.

slide-23
SLIDE 23

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Multi Multi-

  • Effect Distillation

Effect Distillation

slide-24
SLIDE 24

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

MED KEY PARAMETERS MED KEY PARAMETERS

Capital Cost MED 4.5 US$ MM per MIGD Capital Cost –Intake /Outfall 0.1 US$ MM per MIGD

  • f cooling

MED GOR 12 Tons of product/ton

  • f steam

LP Steam Supply 2.5-3 Bar A Lost Power Potential 1.225 MW/MIGD Power Consumption 1.8 KWh/m³ of distillate Steam Consumption 15.8 Tons/MIGD Chemical Costs 40,000 US$/yr per MIGD MED R&R 1% TIC/yr Labor 40,000 US$/yr per MIGD

slide-25
SLIDE 25

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Electrically driven Desalination Electrically driven Desalination Technologies Technologies

  • Reverse Osmosis (RO)

Reverse Osmosis (RO)

  • Vapour Compression Distillation (VCD)

Vapour Compression Distillation (VCD)

  • Hybrids

Hybrids

slide-26
SLIDE 26

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Reverse Osmosis (RO) Reverse Osmosis (RO)

  • Raw seawater total dissolved solids (TDS):

Raw seawater total dissolved solids (TDS): 35 35-

  • 47,000 mg/L

47,000 mg/L

  • Feed pressure: 1000 psia (70 bars)

Feed pressure: 1000 psia (70 bars)

  • Conversion factor: 35%

Conversion factor: 35% -

  • 50%

50%

  • Membrane life: 5 years

Membrane life: 5 years

  • Electrical energy consumption: 4.5 kWh/m

Electrical energy consumption: 4.5 kWh/m3

3

slide-27
SLIDE 27

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

  • Seawater RO has become a mature technology with

Seawater RO has become a mature technology with high degree of reliability. It is using electric energy high degree of reliability. It is using electric energy to operate and with energy recovery devices can to operate and with energy recovery devices can recover 25% to 30% of total energy, from the high recover 25% to 30% of total energy, from the high pressure RO reject brine stream. As a result the total pressure RO reject brine stream. As a result the total plant energy requirements can vary from 4.2 to 7.4 plant energy requirements can vary from 4.2 to 7.4 kWhr kWhr per ton of product. The RO system can vary per ton of product. The RO system can vary some output, but its big advantage is quick start some output, but its big advantage is quick start-

  • up

up allowing its shut allowing its shut-

  • down during peak power operation.

down during peak power operation. The capital cost of the RO plant vary from $3.50 The capital cost of the RO plant vary from $3.50-

  • $6.5.00 per GPD.

$6.5.00 per GPD.

slide-28
SLIDE 28

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

RO KEY PARAMETERS RO KEY PARAMETERS

Capital Cost RO 4.0 US$ MM per MIGD Capital Cost –Intake /Outfall 0.1 US $MM per MIGD feed Power Consumption 5 Kwh/m³ of Permeate Membrane Replacement Rate 20% Per yr RO Chemical Costs 50,000 US$/yr per MIGD RO R&R 2% TIC/yr RO Labor 50,000 US$/yr per MIGD

slide-29
SLIDE 29

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Advantages of Simple Hybrid Advantages of Simple Hybrid MSF MSF-

  • RO Power System

RO Power System

  • A common, considerably small seawater intake can be

A common, considerably small seawater intake can be used used

  • Product waters from the RO and MSF plants are blended

Product waters from the RO and MSF plants are blended to obtain suitable product water quality to obtain suitable product water quality

  • A single stage RO process can be used

A single stage RO process can be used

  • The RO membrane life can be extended

The RO membrane life can be extended

  • Excess power production from the desalting complex

Excess power production from the desalting complex can be reduced significantly, or power to water ratio can can be reduced significantly, or power to water ratio can be significantly reduced be significantly reduced

  • Increase Recovery Ratio

Increase Recovery Ratio

slide-30
SLIDE 30

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

slide-31
SLIDE 31

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Fujeirah Plant Fujeirah Plant -

  • SWRO Racks and

SWRO Racks and Feed Pump/ ER Turbine Arrangement Feed Pump/ ER Turbine Arrangement

slide-32
SLIDE 32

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Power Generation Technologies Power Generation Technologies

  • Back

Back-

  • pressure Steam Turbines

pressure Steam Turbines

  • Extraction Steam Turbines

Extraction Steam Turbines

  • Gas Turbines

Gas Turbines

  • Combined Cycle Plants

Combined Cycle Plants

– – Gas Turbines Gas Turbines – – Steam Turbines Steam Turbines

slide-33
SLIDE 33

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Typical Power to Water Ratios Typical Power to Water Ratios for Different Technologies for Different Technologies

Steam Turbine BTG - MSF PWR = 5.0 Steam Turbine EST - MED PWR = 7.0 Steam Turbine EST - MSF PWR = 10.0 Gas Turbine GT - HRSG - MED PWR = 6.0 Gas Turbine GT - HRSF - MSF PWR = 8.0 Combined Cycle BTG - MED PWR = 10.0 Combined Cycle BTG - MSF PWR = 16.0 Combined Cycle EST - MED PWR = 12.0 Combined Cycle EST - MSF PWR = 19.0 Reverse Osmosis RO PWR = 0.8-1.5 Technology PWR=MW required/Million Imperial Gallons per day

slide-34
SLIDE 34

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Combined Cycle Steam & Power Power for Sale Power to Desal Lost Power Revenue Opportunity SEA Product Water Multi Stage Flash Distillation Feed Brine Reject CW

Traditional Power Desalination

Steam to Desal

slide-35
SLIDE 35

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES Authority

plant

Power contractor Lot P Water contractor Lot D ADWEA

Al Taweelah A2

Siemens Hanjung ADWEA

Al Taweelah A1

Siemens Sidem MEW Oman

Barka

Enelpower Hitachi MEW Qatar

Ras Laffan

Enelpower FI- Italimpianti ADWEA

Shuweihat

Siemens FI- Italimpianti

POWER AND DESALI NATI ON PRI VATE POWER AND DESALI NATI ON PRI VATE PROJECTS I N THE MI DDLE EAST PROJECTS I N THE MI DDLE EAST

slide-36
SLIDE 36

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES Authority Plant Water cap MIGD Power MW Technology Developer ADWEA

Al Taweelah A2

50 710 MSF

CMS

ADWEA

Al Taweelah A1

50 1100 MED

TRACTEBEL TOTALFINA

MEW Qatar Ras Laffan 40 750 MSF

AES

MEW Oman

Barka

30 600 MSF

AES

ADWEA

Shuweihat

100 1500 MSF CMS MEW Oman

Barka

30 500 MSF AES

POWER AND DESALI NATI ON POWER AND DESALI NATI ON PRI VATE PROJECTS I N MI DDLE EAST PRI VATE PROJECTS I N MI DDLE EAST

slide-37
SLIDE 37

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Combined Cycle Steam & Power Power for Sale Power to Desal Product Water Multi Stage Flash Distillation Reverse Osmosis Nanofiltration

New Hybrid Power Desalination

Lost Power Revenue Opportunity Steam to Desal SEA

slide-38
SLIDE 38

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Nanofiltration Nanofiltration NF NF with Multistage with Multistage MSF Flash Process MSF Flash Process

Deaeration Pretreatment Reject Section Recovery Section Brine Heater

Nanofiltration

Seawater Cooling Water Out Reject Soft Feed Recycle Softening Steam Condensate MSF Recycle Blowdown Distillate Makeup Softening

slide-39
SLIDE 39

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Water Security is based on: Water Security is based on:

  • Enough desalination capacity.

Enough desalination capacity.

  • Enough Storage capacity to cover

Enough Storage capacity to cover strategic and seasonal variations. strategic and seasonal variations.

slide-40
SLIDE 40

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Water Supplies are Scarce Water Supplies are Scarce

  • Groundwater

Groundwater reserves are being reserves are being depleted and depleted and becoming more saline becoming more saline

  • There is an increasing

There is an increasing demand due to demand due to population growth, population growth, agricultural needs, agricultural needs, industrialization and industrialization and socio socio-

  • economic

economic improvements improvements

slide-41
SLIDE 41

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Energy is Energy is Power Power Power Power is Water, is Water, Water is Water is Security Security

Combining Combining Desalination and Desalination and Aquifer Storage: Aquifer Storage: The DASR Concept The DASR Concept

slide-42
SLIDE 42

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

  • Electricity demand drops to

Electricity demand drops to 30 30– –40% of peak during the 40% of peak during the winter months winter months

  • Over 50% of power

Over 50% of power generation capacity of generation capacity of power power– – desalination plants desalination plants is idle in winter is idle in winter

  • Idle power can be used to

Idle power can be used to produce low produce low-

  • cost water

cost water (above normal demand) (above normal demand) using using nano nano-

  • filtration and

filtration and

  • ther membrane
  • ther membrane

desalination technologies desalination technologies

Creating Additional Water Creating Additional Water

slide-43
SLIDE 43

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

GAS to Power, Power to Seawater GAS to Power, Power to Seawater Desalination and Storage/Aquifer Desalination and Storage/Aquifer Storage and Recovery (DASR) Storage and Recovery (DASR)

Power Generation Water desalination Water grid Power grid

Underground Gas Fresh water - underground

slide-44
SLIDE 44

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

BESI X LEADI NG EDGE WATER BESI X LEADI NG EDGE WATER TECHNOLOGI ES TECHNOLOGI ES MI SSI ON MI SSI ON

E ECONOMI CALLY CONOMI CALLY I NCREASE I NCREASE THE OUTPUT OF THE OUTPUT OF MSF MSF PLANTS BY PLANTS BY: :

  • ADDI NG THE

ADDI NG THE LET NF LET NF SYSTEM SYSTEM

  • O

OPTI MI ZI NG MSF PLANT PERFORMANCE PTI MI ZI NG MSF PLANT PERFORMANCE

  • CUTI NG CAPI TAL COSTS BY AT LEAST 25%

CUTI NG CAPI TAL COSTS BY AT LEAST 25%

  • NO NEED FOR NEW I NTAKE AND POWER PLANT

NO NEED FOR NEW I NTAKE AND POWER PLANT

The Nanofiltration system will utilize The Nanofiltration system will utilize idle electricity for production of water idle electricity for production of water at low marginal cost of power at low marginal cost of power. .

slide-45
SLIDE 45

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Growth for I ntegrated Hybrid Growth for I ntegrated Hybrid

  • Increasing capacity of existing plants

Increasing capacity of existing plants – – upgrade alongside rehab upgrade alongside rehab

  • NF able to capitalize on the effluent water

NF able to capitalize on the effluent water

  • Provide new plants with a clear advantage

Provide new plants with a clear advantage through a better IGD/$ invested (Capex) through a better IGD/$ invested (Capex)

  • Reduce power to water ratio (Kwh/IGD)

Reduce power to water ratio (Kwh/IGD)

  • Improve thermal and membrane based

Improve thermal and membrane based processes processes

slide-46
SLIDE 46

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Benefits Benefits of Nanofiltration

  • f Nanofiltration
  • PREFERENTI ALLY REMOVES SCALI NG

PREFERENTI ALLY REMOVES SCALI NG (DI VALENT) I ONS (DI VALENT) I ONS

  • ALLOWS HI GHER TOP BRI NE

ALLOWS HI GHER TOP BRI NE TEMPERATURE FOR MSF (121 vs. 110 TEMPERATURE FOR MSF (121 vs. 110 ° ° C) C)

– – Higher Flash Range I ncreases Production

Higher Flash Range I ncreases Production

– – Reduced MSF Capital Costs

Reduced MSF Capital Costs

– – Reduced MSF Operating Costs

Reduced MSF Operating Costs

slide-47
SLIDE 47

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

THE SEWA CASE of THE SEWA CASE of I NTEGRATED HYBRI D I NTEGRATED HYBRI D

  • I NCREASE 44% THE CAPACI TY OF

I NCREASE 44% THE CAPACI TY OF EXI STI NG MSF FROM 5 MI GD to 7.2 MI GD EXI STI NG MSF FROM 5 MI GD to 7.2 MI GD

  • MI MI MUM FOOT PRI NT, NO ROOM FOR

MI MI MUM FOOT PRI NT, NO ROOM FOR NEW DESALI NATI ON PLANTS NEW DESALI NATI ON PLANTS

  • REDUCE OPERATI NG COST

REDUCE OPERATI NG COST

  • NO CHANGES TO I NTAKE STRUCTURE

NO CHANGES TO I NTAKE STRUCTURE

  • NO I NCREASE I N POWER FACI LI TI ES

NO I NCREASE I N POWER FACI LI TI ES

  • CUTTI NG MSF CAPI TAL COST FOR

CUTTI NG MSF CAPI TAL COST FOR ADDI TI ONAL CAPACI TY BY 40% ADDI TI ONAL CAPACI TY BY 40%

slide-48
SLIDE 48

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

PLANT OPTI MI ZATI ON I S BASED ON: PLANT OPTI MI ZATI ON I S BASED ON:

  • COMPUTER SI MULATI ON

COMPUTER SI MULATI ON OF PLANT OF PLANT OPERATI ONS OPERATI ONS RESULT RESULTI NG I N: I NG I N: PLANT PLANT MODI FI CATI ONS TO I NCREASE WATER MODI FI CATI ONS TO I NCREASE WATER PRODUCTI ON PRODUCTI ON AND AND I MPROVI NG I MPROVI NG EFFI CI ENCY EFFI CI ENCY

  • COMPREHENSI VE ENGI NEERI NG REVI EW

COMPREHENSI VE ENGI NEERI NG REVI EW

slide-49
SLIDE 49

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Investment Costs Comparison Investment Costs Comparison

3.4 3.4 5.0 5.0 Total Investment Total Investment N/A N/A 0.7 0.7 Intake Intake 2.3 2.3 3.3 3.3 Desalination plant Desalination plant 3.4 3.4 4.3 4.3 Total Direct Investment Total Direct Investment 0.1 0.1 0.1 0.1

  • Misc. and commercial
  • Misc. and commercial

0.25 0.25 0.9 0.9 Civil & Engineering Civil & Engineering 0.5 0.5 N/A N/A MSF modifications MSF modifications NF + MSF NF + MSF RO RO $ inv / IGD $ inv / IGD

slide-50
SLIDE 50

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Unit Cost Analysis Unit Cost Analysis

0.226 0.226-

  • .234

.234 0.268 0.268 Operating Costs Operating Costs 0.403 0.403-

  • .479

.479 0.598 0.598 Total Total 0.177 0.177-

  • .245

.245 0.330 0.330 Annual Investment return * Annual Investment return * NF + MSF NF + MSF $ / m $ / m³ ³ RO RO $ / m $ / m³ ³

* Based on a 20 year life and 6% interest rate

slide-51
SLIDE 51

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

slide-52
SLIDE 52

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

slide-53
SLIDE 53

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

slide-54
SLIDE 54

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

slide-55
SLIDE 55

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Improvements in distillation and Improvements in distillation and membrane processes membrane processes

  • R. Borsani in the presentation
  • R. Borsani in the presentation “

“MSF I nnovation

MSF I nnovation – – Beyond Large Size Unit Beyond Large Size Unit” ” at the IDA Forum on

at the IDA Forum on Innovation and Integration in Desalination Dubai Innovation and Integration in Desalination Dubai described the new frontiers, as described the new frontiers, as

  • TOP BRINE TEMPERATURE : The Increase of TBT can

TOP BRINE TEMPERATURE : The Increase of TBT can Allow Higher Production With Almost Same Desal Trains Allow Higher Production With Almost Same Desal Trains

  • HYBRIDISATION : The Application Of Hybrid

HYBRIDISATION : The Application Of Hybrid Technologies (MSF + RO Or MSF + MED) Can Improve Technologies (MSF + RO Or MSF + MED) Can Improve Overall Efficiency Overall Efficiency

  • THERMAL IMPROVEMENT : New MSF Schemes And

THERMAL IMPROVEMENT : New MSF Schemes And Ancillary Equipment. Ancillary Equipment.

slide-56
SLIDE 56

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

LET LET Proprietary Proprietary

Makeup Makeup Pump Pump Distillate Distillate Product Product Recycle Recycle Pump Pump Brine Brine Blowdown Blowdown Pump Pump Brine Brine Discharge Discharge Vacuum Vacuum De De-

  • aerator

aerator Brine Brine Heater Heater Condensate Condensate Return Return RO RO Membranes Membranes RO Energy RO Energy Recovery Recovery RO RO Permeate Permeate RO Feed RO Feed Pump Pump

HYBRID WITH NF PRIOR TO MSF

Seawater Seawater Discharge Discharge Pre Pre-

  • treatment

treatment NF NF Array Array NF Feed NF Feed Pump Pump NF, RO, NF, RO, MSF Brine MSF Brine LP LP LP LP St Steam St Steam Po Potable Po Potable Wa Water Wa Water Bypass Bypass Sea eawater Sea eawater Supp Supply Sup Supply Seawater Seawater Pump Pump Chemicals Chemicals

slide-57
SLIDE 57

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Potential for MED technology Potential for MED technology improvements. improvements.

At IDA Forum on Innovation G. Canton in At IDA Forum on Innovation G. Canton in presentation presentation “ “The Recent Progress and Next The Recent Progress and Next Generation of MED Plants Generation of MED Plants” ” outline the significant

  • utline the significant

growth and potential for the Multi growth and potential for the Multi-

  • effect distillation

effect distillation

  • technology. The 8 MIGD MED, plant started
  • technology. The 8 MIGD MED, plant started

production in Sharjah August 2006, it is the largest production in Sharjah August 2006, it is the largest single unit and 10X 6 MIGD= 60 MIGD Hidd single unit and 10X 6 MIGD= 60 MIGD Hidd-

  • Bahrain plant awarded is the world largest MED

Bahrain plant awarded is the world largest MED plant. plant.

slide-58
SLIDE 58

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Future Developments Future Developments

  • Further reduction of $ invested / IGD to

Further reduction of $ invested / IGD to $2.5/IGD through optimization $2.5/IGD through optimization

– – Introduction of UF/MF as pre treatment Introduction of UF/MF as pre treatment

  • Reduce operating costs through

Reduce operating costs through

– – Energy reduction Energy reduction – – energy recovery, one pass energy recovery, one pass – – Chemical reduction Chemical reduction

  • NF for MED

NF for MED

  • NF for RO

NF for RO

slide-59
SLIDE 59

BESIX LEADING EDGE WATER TECHNOLOGIES BESIX LEADING EDGE WATER TECHNOLOGIES

Energy is Power, Power is Water, Water is Security