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close this bookManaging Water for Peace in the Middle East: Alternative Strategies (UNU, 1995, 309 pages)
close this folder2. Review studies on arid-zone hydrology and water-resources development and management
View the document2.1 The arid zone in global atmospheric circulation water resources
View the document2.2 The Tigris and Euphrates Rivers
View the document2.3 The Indus River
View the document2.4 The Nile River
View the document2.5 The Jordan River
View the document2.6 The Colorado River
View the document2.7 Non-renewable groundwater development in the Middle East
View the document2.8 Brackish-groundwater reverse-osmosis desalination in Bahrain
View the document2.9 Seawater desalination in the Arabian Gulf countries
View the document2.10 Groundwater-hydro development in Chile and Libya
View the document2.11 Mediterranean-Qattara solar-hydro and pumped-storage development
View the document2.12 Concluding remarks

2.9 Seawater desalination in the Arabian Gulf countries

Owing to the rapid increase in demand for water in the Arabian Gulf countriesSaudi Arabia' Kuwait, the United Arab Emirates, Qatar, Bahrain, and Omanwhere conventional water resources such as fresh surface water and renewable groundwater are extremely limited, other alternatives such as wastewater reclamation and desalination have been adopted since the 1960s. Countries such as Saudi Arabia, Kuwait, Qatar, and Bahrain all use nonrenewable groundwater resources in large quantity, causing depletion of these valuable resources and deterioration in the quality of water. Although conventional water resources such as renewable groundwater and surface runoff are available in countries like Oman, the United Arab Emirates, and Saudi Arabia, these resources still need to be properly developed in an integrated water-resources planning context.

In some of the more arid parts of the Middle East, in particular the Gulf states, where good quality water is not available or is extremely limited, desalination of seawater has been commonly used to solve the problems of water supply for municipal and industrial uses.

Kuwait was the first state to adopt seawater desalination, linking electricity generation to desalination. The co-generation station, as it is called, re-uses low pressure steam from the generator to provide energy for the desalination process. As a result, both energy and costs are minimized. Kuwait began desalinated water production in 1957, when 3.1 million m³ were produced per year. By 1987 this figure had risen to 184 million m³ per year.

In Qatar, too, an intensive programme of desalinated water production has been started, which should be supplying about 150 million m³ of water per year by the year 2000. This is believed to be about threequarters of the total water demand, with the rest to be supplied from groundwater sources, which are mostly brackish. About half of the country's demand will be generated in the urban/industrial centres.

Saudi Arabia entered the desalinated water field much later than Kuwait. The first plant was commissioned in 1970. It has, however, gone in for an ambitious programme of desalination plant construction on both the Red Sea and Gulf coasts. The Saline Water Conversion Corporation had installed 30 desalination plant projects by the end of the 1980s. The total production of desalinated water is estimated to be 2.16 million m³ (572 million [US] gal.) per day including a facility at Al-Jubail producing 1 million m³ per day, which is currently the world's largest distillation plant.

In spite of the high cost of seawater desalination, with unit water costs five to ten times as high as those of conventional water-resources development, a vast quantity has been produced to meet the increasing demand for domestic water in the Arabian Gulf countries. As in Kuwait, however, there is increasing government concern about the production cost of desalinated water, and every effort is being made to ensure that water use is as efficient as possible.

2.9.1 Installed capacity of desalination plants

There are about 1,483 desalination units operating in the Arabian Gulf countries, which account for 57.9% of the worldwide desalting plant capacity. The dominant plant type is multi-stage flash (MSF) which accounts for 86.7% of the desalting capacity, while the reverse osmosis accounts for only 10.7%. The installed capacity of desalination plants in the Arabian Gulf countries is estimated at 5.76 million m³ per day in total, including 2.98 million m³ in Saudi Arabia, which is approximately half of the total desalination capacity of the Gulf countries (Al-Mutaz 1989). The installed capacity with shares of each process are shown in table 2.10.

MSF desalting has proved to be the simplest, most reliable, and most commonly used seawater system in large capacities. It has reached maturity with very little improvement in sight. This maturity is expressed in reliable designs of large units up to 38,000 m³ (10 million gal.) per day, long operation experience with high on-line stream factors (up to 95%), confidence in material selection, and very satisfactory water pre-treatment. However, there has been a recent trend towards the use of reverse osmosis in seawater desalination, both for new plants and in connection with the present MSF plants, taking into account the possible reduction in energy requirements and the lower operation and maintenance cost for RO.

Table 2.10 Installed capacity of desalting plants and share by process type in the Arabian Gulf countries

  No. of units Capacity (1,000 m³/day) Share by process type (%)
MSF RO ED VC MED
Saudi Arabia 874 2,980 80.7 16.2 2.6 0.5  
Kuwait 279 1,090 95.5 1.8 0.55 1.6 0.25
U.A.E. 99 1,020 98.3 0.9 0.5 - -
Qatar 47 310 9 7.9 - - 0.7 0.9
Bahrain 143 260 56.7 37.2 4.9 0.8 0.4
Oman 41 100 91.1 1.9 0.9 1.7  
TOTAL 1,483 5,760 86.7 10.7 1.8 0.65 0.15

Source: Akkad 1990.
MSF = multi-stage flash. RO = reverse osmosis. ED = electrodialysis. VC = vapour compression. MED = multi-effect distillation.

2.9.2 The world's largest seawater desalination with high-pressure pipeline system

To meet the water demands of the increasing population and water short regions in Saudi Arabia, the Saline Water Conversion Office (SWCO) under the Ministry of Agriculture and Water was made responsible for providing fresh water by desalination of seawater in 1965. The first seawater desalination plant was commissioned in 1970. With its increasing responsibilities to provide fresh water, the SWCO was changed in 1974 into an independent corporation, the Saline Water Conversion Corporation (SWCC), which then developed an elaborate plan to construct dual-purpose plants on both the east and west coasts of the kingdom.

The SWCC had constructed 24 plants by 1985, including 17 plants on the western coast along the Red Sea, from Haql on the Gulf of Aqaba in the north to the tiny Farasan island in the south, and 7 plants on the east coast along the Arabian Gulf from Al-Khafji to Al-Khobar (fig. 2.48). These plants were producing 1.82 million m³ (481 million gal.) of fresh water per day and 3,631 MW of electric power. By the end of the 1980s the total production of fresh water was estimated to have been increased to 2.17 million m³ (572 million gal.) of fresh water per day and 4,079 MW of electric power by the addition of six cogeneration plants (SWCC 1988).



Fig. 2.48 Desalinsation plants and water supply in Saudi Arabia

In addition to desalination and power plants, the SWCC provides water to inland regions by means of pipelines. The Al-Jubail-Riyadh pipeline is one of the world's largest water pipeline systems with seawater desalination plants. The pipeline has a diameter of 1.5 m (60 inches), a length of 466 km, a differential head of 690 m, and a pumping capacity of 830,000 m³ per day (SWCC 1988).

2.9.3 Cost constraints of seawater desalination

The MSF process has served very well during the past ten years, especially in the Middle East. During this period, operating experience has been developed that should result in substantial extensions to what was heretofore considered a reasonable operating life. Certainly this favourable experience will be a factor in the selection of future plants.

However, the lower capital and operating costs for the RO process should receive increasing attention in the selection of a desalination process in coming years. There are still opportunities for further lowering of costs through improved membrane technology, notably in increasing membrane life. Another new development with good potential for reducing costs for the RO process are membranes for operating at high pressures up to 1,500 psi (105 kg/cm²) and 50% conversion when operating on seawater with 45,000 mg of TDS per litre.

Another alternative process will be low-temperature multi-effect horizontaltube evaporators. If aluminium tubes and tube sheets can be shown to have a reasonable life in Middle East seawater, the capital cost can be reduced, or a higher performance ratio can be achieved.

Another factor which will favour reverse osmosis in coming years is that it is the most energy-efficient of all of the processes. This will be of increasing importance if in fact fuel-oil prices rise further as expected and environmental considerations increase in importance. The cost of energy consumption is also the largest single item in the cost of desalted water. It is significant that, for either a single-purpose or a dual-purpose plant, RO appears to be the most cost-effective. On the basis of world fuel costs in 1989, the RO process would save over 10% compared with multi-effect distillation and 32% compared with MSF (Leitner 1989).

2.9.4 Hybrid RO/MSF seawater desalination to compromise quality-cost constraints

It seems that the race for the second generation of seawater desalters has been settled, with RO and low-temperature multi-effect horizontal tube evaporators as front runners. Both systems are characterized by their low energy requirements compared with the MSF system. As shown in fig. 2.49, which gives the worldwide market shares of various desalination processes, RO accounted for 65% of market share in 1987 (Wangnick and IDA 1988). Beside these two options, there are combination possibilities of different desalting plant types. In the hybrid MSF/RO desalination-power process, a seawater RO plant is combined with either a new or existing dualpurpose MSF plant with the following advantages:



Fig. 2.49 World market share of various desalination processes (Source: Wangnick and IDA 1988)

>> The capital cost of the combined RO/MSF plant can be reduced.

>> A common seawater intake is used.

>> Product waters from the RO and MSF plants are blended to obtain suitable product-water quality. Taking advantage of the fact that the MSF product (25 mg of TDS per litre) typically exceeds potable water specifications (WHO standard: 500-1,000 mg/l the product water specification in the RO system can thereby be reduced.

>> A single-stage RO process can be used and the RO membrane life can be extended because of the reduced product-water specification. (The life of the RO membrane can be extended from three to five years, or the annual membrane replacement cost can be reduced by nearly 40%.)

>> Electric power production from the MSF plant can be efficiently utilized in the RO plant, thereby reducing net export power production. In addition, the electric power requirement to drive the high-pressure pumps of the RO system, which is a major factor of energy consumption, can be reduced by 30% by adding an energy recovery unit to the brine discharge in the RO system. (Power consumption for a single-stage seawater RO plant at 30% of recovery/conversion is estimated to be 9.24 kWh/m³ without or 6.38 kWh/m³ with energy recovery on brine discharge [Awerbuch et al. 1989].)

>> Blending with RO product water reduces the temperature of the MSF product water. A problem common in areas in the Middle East is the high temperature of the product water. RO for high pressure brine when no energy recovery is used can be used to cool the MSF product water with an eductor.

JEDDAH RO/MSF HYBRID PROJECT. The first large-scale MSF/RO hybrid project, the Jeddah I rehabilitation project in Saudi Arabia, is now in operation by the Saline Water Conversion Corporation. This 15 million gal. (56,800 m³) per day RO plant, the world's largest facility for seawater conversion, has demonstrated the attractiveness of the hybrid concept. The Jeddah I MSF desalination plant was completed in 1970, with an installed capacity of 5 million gal. (18,925 m³) per day. It was one of the world's largest plants in the early 1970s and therefore has a significant place in history. The installed capacity of the Jeddah desalting complex was expanded by steps to a nominal capacity of 85 million gal. (321,725 m³) per day, all by MSF.

In 1985 the operation and maintenance of the Jeddah I MSF plant had become increasingly costly. To keep pace with the increasing water demand, the 5 million gal. per day Jeddah I MSF plant was replaced by a 15 million gal. per day RO plant (phase I) in 1986-1989, which is incorporated in a hybrid RO/MSF desalination system. The RO unit has the following design criteria (Muhurji et al. 1989):

  • feed-water quality: TDS = 43,300 mg/l chloride as Cl- = 22,400 mall, pH = 8.2, water temperature 24.5-32.5°C;
  • operating pressure at 60 kg/cm² (maximum design pressure: 70 kg/ cm );
  • a single-stage design, including 10 RO trains, with each train including 148 RO modules;
  • hollow fine fibre (Toyobo Hollosep made of cellulose triacetate) RO module with 10 inch diameter;
  • recovery ratio of 35% of product water;
  • product-water salinity as specified at 625 mg of chloride per litre (= 1,250 mg of TDS per litre).

Since MSF product water has a salinity as low as 25-50 mg of TDS per litre, the salinity of the permeate from the Jeddah I RO plant (phase I) was specified as 625 mg of chloride (1,250 mg of TDS) per litre, which is a major factor in minimizing the cost of the RO. In a cost analysis done by Bechtel (Muhurji et al. 1989), it was shown that the product water cost from the RO system in a hybrid MSF/RO plant can be reduced by 15% compared with a stand-alone RO plant.