O Technical and Economic Evaluation of Seawater MSF and RO Desalination Processes for Madinat Yanbu - PowerPoint PPT Presentation

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O Technical and Economic Evaluation of Seawater MSF and RO Desalination Processes for Madinat Yanbu

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Process Steam and Power Availability. Product Water Requirement. Energy Efficiency ... scale control and tube cleaning methods have increased operational periods ... – PowerPoint PPT presentation

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Title: O Technical and Economic Evaluation of Seawater MSF and RO Desalination Processes for Madinat Yanbu


1
O Technical and Economic Evaluation of Seawater
MSF and RO Desalination Processes for Madinat
Yanbu Al-SinaiyahAuthors A. Khawaji, J. Wie
and A. Al-MutiriIDA World Congress, Bahrain 2002
  • Presented By
  • Fawaz Al-Ghamdi
  • May 22, 2007

2
OUTLINE
  • Introduction
  • Technical Comparison
  • Cost Comparison
  • Cost Comparison For The New Unit
  • Conclusion

3
INTRODUCTION
  • The Royal Commission for Jubail And Yanbu
    maintain and operate Madinat Yanbu Al-Sinaiyah
    (MYAS) including the seawater desalination plant
  • The existing desalination plant used to support
    community and industry
  • Consist of six 380 m3/hr multi-stage flash (MSF)
    unit
  • Because of the expected growth of the MYAS
    community and industry, additional seawater
    desalination unit will be required to meet the
    future demand.
  • Two major commercial seawater desalination
    process in the area RO and MSF
  • In RO Saudi Arabia 4 Large size, Others are
    small

4
INTRODUCTION
  • Objective
  • The objective of this paper is to present
    the results of the technical and economic
    evaluation of the MSF and RO processes and select
    the one that suit MYAS

5
INTRODUCTION
6
INTRODUCTION
7
TECHNICAL COMPARISON
  • MSF system is based on the proved technology and
    have demonstrated operational reliability over
    two decades in the Middle East and throughout the
    world
  • RO system is increasingly gaining in popularity
    due to simplicity, improved performance,
    capability to handle a wide variety of feed
    water, energy efficiency, less space , less time
    to construct, less manpower required.

8
TECHNICAL COMPARISON
  • Major Technical Aspects
  • Process Steam and Power Availability
  • Product Water Requirement
  • Energy Efficiency
  • Sea Water Feed Condition

9
TECHNICAL COMPARISON
  • Process Steam and Power Availability
  • There are 5 HRSG supply steam and power
  • Provision have been made to supply emergency
    steam from STG since it was anticipated that the
    new desalination unit would reduce the
    availability steam to generate electric power.
  • Steam Supply for the new unit is adequate.

10
TECHNICAL COMPARISON
  • Product Water Requirement
  • Product water specification is based on the
    required process water quality needed for plant
    equipment.
  • If new MSF units is installed, it will meet the
    process water requirement.
  • Single stage RO plant is adequate to produce
    water with TDS lt 435 ppm with 99 recovery. So,
    more than one stage will be required.

11
TECHNICAL COMPARISON
  • Energy Efficiency
  • RO plants require only electrical power to run
    the high pressure pumps. (7-8.3 Kwh/m3 of
    product water)
  • MSF units require thermal and electrical energy,
    the total consumption is approximately 17 Kwh/m3
    of product water.

12
TECHNICAL COMPARISON
  • Seawater Feed Condition
  • Conditions of seawater are safe for operation of
    both MSF and RO plants since the sea water
    condition is stable.
  • An MSF plant would require 3 times more seawater
    than an RO plant equivalent in size.

13
TECHNICAL COMPARISON
  • Advantages and Disadvantages
  • Major advantages of the MSF desalination plants
    are as follows
  • 1) Demonstrated operational reliability over
    twenty years in the Kingdom and throughout the
    world.
  • 2) Relatively insensitive to the salinity of the
    feed water with production of high quality water
    (less than 10 ppm TDS), which is more suitable
    for use as process water.
  • 3) Minimum requirement of feed water
    pretreatment. Unaffected by normal levels of
    suspended or biological matters in the seawater.

14
TECHNICAL COMPARISON
  • Advantages and Disadvantages
  • Major advantages of the MSF desalination plants
    are as follows
  • 4) In the winter time as the seawater temperature
    declines, the flash range can be increased
    resulting in higher production of desalinated
    water.
  • 5) The use of improved scale control and tube
    cleaning methods have increased operational
    periods between shutdowns, thereby increasing
    plant availability.

15
TECHNICAL COMPARISON
  • Disadvantages Of MSF
  • 1) Relatively higher costs in both capital cost
    and OM cost.
  • 2) Require more energy (both electrical and
    thermal energy) than RO Plants.
  • 3) Require more seawater (about three times more)
    than RO Plants
  • 4) Require larger space for a given capacity
    plant.
  • Encounter more corrosion problems than RO plants
  • Longer construction time.

16
TECHNICAL COMPARISON
  • Advantages of RO
  • 1) Relatively lower capital cost because of
    simpler system.
  • 2) Less overall energy consumption
  • 3) Require about one third the seawater needed
    for MSF plants.
  • 4) Operate at ambient temperature without any
    adverse impact on environment (i.e. thermal
    pollution).
  • 5) Scheduled maintenance can be performed without
    shutting down the entire plant because of modular
    design.
  • 6) Use more plastics and non-metals, therefore
    reducing corrosion related problems.

17
TECHNICAL COMPARISON
  • Advantages of RO
  • 7) Less space requirement than a similar capacity
    MSF Plant.
  • 8) Has fewer components, resulting in less repair
    and replacement parts.
  • 9) Faster startup and shutdown
  • 10) Shorter construction time
  • 11) Easier capacity increase for future expansion

18
TECHNICAL COMPARISON
  • Disadvantages of RO
  • 1) Predominant cause of most failures is
    unsatisfactory pretreatment of feed water.
    Therefore, RO Plants require constant attention,
    careful monitoring and good attitude by operating
    personnel.
  • Biological activity of the seawater feed system
    must be kept under rigid control, as opposed to
    MSF plants
  • Chemical addition for pretreatment must be
    carefully monitored and adjusted to match the
    seasonal change in seawater quality.
  • 4) Membrane performance monitoring should be
    rigidly followed to satisfy the manufacturers
    warranty requirements.
  • RO membranes are expensive.

19
COST COMPARISON
  • Based on literature review, the cost ratios for
    MSF and RO

20
COST COMPARISON
  • The various factors that are significant in
    comparing the production cost of water in MSF and
    RO include
  • Energy Cost
  • Chemicals Cost
  • Metals Cost
  • Membrane Replacement Cost
  • Land Use Cost
  • Construction time
  • Fuel Price

21
COST COMPARISON
  • Energy Cost
  • RO 7 Kwh/m3
  • MSF 17 Kwh/m3
  • Chemicals Cost
  • The cost of chemicals in an RO plant is higher
    than that of chemicals in an MSF Plant, depending
    on the pretreatment and scale control method
  • Metal Cost
  • Many of the corrosion problems encountered with
    MSF plants in the past have been overcome by
    selection of improved materials, and a s a
    result, MSF plants can be adversely affected by
    the high cost of alloy material
  • The high pressure pumps and piping in RO unit
    requires stainless steel material.

22
COST COMPARISON
  • Membrane Replacement Cost
  • Only applicable to RO plants
  • Average life 5 years
  • An accurate membrane replacement frequency is
    difficult to predict as it is tied up with
    feedwater treatment and operation.
  • Land Use and Construction
  • RO uses less land and its construction time is
    shorter than an MSF plant
  • Fuel Price
  • Related to energy
  • RO is more energy efficient process

23
COST COMPARISON FOR THE NEW UNIT
Estimated Water Production Cost
24
COST COMPARISON FOR THE NEW UNIT

25
CONCLUSIONS
  • This evaluation of MSF and RO is not to establish
    superiority of one system or technology over the
    other, but to select a process based on its cost
    effectiveness, simplicity in operation and
    maintenance, and compliance with the requirement
    for potable water
  • For the production of potable water of a 570
    m3/hr, the capital cost for s single stage RO
    plant is estimated to be about 27 percent lower
    that an identical size MSF plant
  • Ro is more energy efficient that MSF
  • RO unit chemical costs were determined to be
    lower that those of the MYAS MSF plant


26
CONCLUSIONS (cont.)
  • Sea water requirement for RO unit is about 1/3
    sea water requirement for the MSF unit.
  • RO plants require less space, less construction
    time and more flexible
  • RO unit have not adverse impact in environment as
    it is operate at atmospheric temperature
  • As a result of this evaluation, RO is determined
    to be more cost-effective in both initial capital
    cost and water production cost
  • On the basis of this evaluation and the best
    available data, a decision was made to install a
    seawater RO plant at MYAS


27
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