DISTRICT COOLING & DESALINATION USING HEATPUMPS & M.E.D. · District Cooling and Desalination...
Transcript of DISTRICT COOLING & DESALINATION USING HEATPUMPS & M.E.D. · District Cooling and Desalination...
DISTRICT COOLING & DESALINATION USING HEATPUMPS & M.E.D.
David Pearson Director of Innovation
Star Refrigeration
Imtiaz Khan Regional Manager, Energy
(Power, Oil & Gas) Alfa Laval Middle East Ltd
History & Experience Why bother?
60% of GCC electricity is for cooling
= 82GW * 0.6 = 49.2GW
@ COP = 3.0 = 200GW of waste heat
= 1,752,000GWh
1,000 Million Barrels of crude oil EVERY YEAR!!! thrown away
More than output of some GCC countries!
Desalination systems are established technology
How district cooling can be joined with desalination?
The equipment used for the cooling
The value of this solution
The secondary benefits
Desalination delivering 40% savings in water cost
History & Experience Agenda:
• 1954 Pioneer with first Desalination unit onboard a ship – shell & tube design
• 1967 Design with Titanium plates as evaporator heat transfer surface
Today • Supplied more than 30,000 units
of the plate desalination concept • More than 850,000 m3/d in accumulated
capacity • Average 1000 units per year is delivered • Market share leader with 70 % market share
achieved and sustained for marine and offshore
History & Experience Marine Applications Desalination Milestones
• Building on a Proven Foundation
• 1988 Decision to Develop a plate desalination concept for large scale capacities
• 1992 Commercial introduction of the Titanium plate desalination concept
• Received orders for more than 200 new plate type desalination units.
• More than 100,000 m3/d capacity installed
• With successful implementation of the concept, significant number of references has been achieved in all parts of the World
History & Experience Land Applications Desalination Milestones
Example of desalination installation
References Round the Globe World wide Alfa Laval Experience
2 x MEP-7-6840 & 1 x 60% Dump Condenser Module
Karachi – Pakistan Sea Water Distillation. Karachi – Pakistan
2 x MEP-7-6840 & 1 x 60% Dump Condenser Module
“Iskenderun Bay” Turkey 3 x TVC-4-1750
Kaltim - Indonesia 2xTVC-3-1680 (2 x 1,680 m3/day)
Kansai Electric (KEPCO), Nuclear Power Plant, Takahama, Japan; 2x TVC-4-1000; 2x 1,000 m3/day, 2002
High quality water for Prawn production
National Prawn, Saudi Arabia MED-5-425 - 475 m3/day 2002
Binzagr CO-RO produce soft drinks and beverages using freshwater distillated from underground water, which has a higher salinity chemical complexity than the Red Sea
Binzagr CoRo, Jeddah, VVC-350 & VVC-125: 475 m3/day
Plate type Tubular
Performance %
1 2
125
100
75
Time
Performance through time Alfa Laval Plate type evaporators can be cleaned 100% Tubular evaporators gradually decrease performance because of “irreversible” scaling/fouling
CIP cleaning can remove alkaline soft scaling, and hard scaling can also be removed 100% in a PHE type desalination unit.
Why use Plate MED?
Stephen Appleton, Director Ramboll 2010
Energy Security
Climate Change
Water supply
"The three issues which will have the greatest impact on humanity over the next century are
The future!!!!!.
Think Differently-District Cooling and Desalination
• A solution to this would be through the use of ammonia refrigeration heat pumps serving district cooling networks, with waste heat being
utilised for desalination purposes.“
Stephen Appleton, Director Ramboll 2010
90˚C Ammonia Heatpump
The World’s Largest 90C Natural Heatpump?
District Cooling and Desalination Solution?
Use waste heat from the cooling plant. Example District Cooling
COPc = 5.0
10MW Cooling
2MW Power
12MW Waste Heat
Combined DC and Desalination
COPc = 2.6
10MW Cooling
3.85MW Power (extra 1.85MW)
13.85MW Waste Heat
COPhi = 13.85/1.85 =7.48
87% of energy is waste heat
60% of GCC electricity is for cooling = 82GW * 0.6 = 49.2GW
@ COP = 3.0 = 200GW of waste heat = 1,752,000GWh
1,000 Million Barrels of crude oil EVERY YEAR!!! thrown away
More than output of some GCC countries!
District Cooling and Desalination
District Cooling and Desalination Solution?
Use waste heat from the cooling plant. Large District Cooling
350MW Cooling
700,000 litres/hr water USE
Combined DC and Desalination
350MW Cooling
3,181,000 litres/hr of purified water PRODUCTION
OR
4.54 x self consumption
Delivering over 40% savings in water cost
District Cooling and Desalination
NeatDesal
Proven
Turning waste heat from cooling into water.
Think Differently-District Cooling and Desalination
Demystifying!!.HFCs are not GOOD!
Although, replacing ozone depleting substances with HFCs helps to protect the ozone layer, the increasing use of high-GWP HFCs is likely to undermine the very significant
climate benefits achieved by the Ozone Depleting Substance phase-out to date.
HFCs: A Critical Link in Protecting Climate and the Ozone Layer
Published by the United Nations Environment Programme (UNEP), November 2011 ISBN: 978-92-807-3228-3
Demystifying!!.HFCs are not GOOD!
Although, replacing ozone depleting substances with HFCs helps to protect the ozone layer, the increasing use of high-GWP HFCs is likely to undermine the very significant
climate benefits achieved by the Ozone Depleting Substance phase-out to date.
HFCs: A Critical Link in Protecting Climate and the Ozone Layer
Published by the United Nations Environment Programme (UNEP), November 2011 ISBN: 978-92-807-3228-3
Don’t forget Refrigerant Global Warming Potentials
Leakage!!!.
R134a is odourless and WILL leak undetected.
If we assume 1% per year!!..
A 350MW system will have approx 150,000Kg R134a
So leakage will be 1500Kgs per year.
This costs!!!.$60,000 per year in 2011....or more
Doubling every 2-3 years so by 2030 maybe $1.8M
And @ 1300 GWP = 1,850,000 kgs of Carbon Dioxide
=6.96 million miles in a VW Golf
28 x times around the World!
Refrigerant Global Warming Potentials
GWP
R22 R134a R407C R410A
2000
0
1500
1000
500
R717
Beware of the Refrigerant Timeline
1970 1975 1980 1985 1990 2000 1995
Aware ozone depletion CFC phase-out
Montreal protocol CFC ban
1970 1975 1980 1985 1990 2000 1995
Refrigerant Timeline
Aware ozone depletion
Montreal protocol CFC ban
2005 2010 2020 2015
Refrigerant Timeline
1990 1995 2000 2005 2010 2020 2015
Aware ozone depletion
Montreal protocol CFC ban
HCFCs
HCFC ban
Virgin HCFC ban
£
Refrigerant Timeline
1990 1995 2000 2005 2010 2020 2015
Aware ozone depletion
Montreal protocol CFC ban
HCFCs HFCs
Leakage
HCFC ban
R717 EU F-Gas
regs
£
HFC emissions may also be substantial when compared to future levels of CO2 emissions.(28-45%)-UNEP
District Cooling and Desalination
NeatDesal
Proven parts
Turning waste heat from cooling into water.
AND SAVING OPEX AND EMISSIONS
Steam or hot water SG
MEP Process
Corrugated plate design promotes High turbulence with
• Efficient heat transfer • 3-5 times higher in liquid/liquid applications • 2-3 times higher in 2-phase applications
• Minimised fouling • 5-10 times higher wall shear stress
Hot Medium
Cold Medium
Plate heat Exchanger (PHE) Channel design
Multiple Effect Process
Vessel Internal: - Pressure Plate - Plate Pack - Sea Water distribution
Multiple Effect Process
How do we “Raise“ heat from 2C to 90C?
Interstage @ 58C
HOR = 14.05MW
R eff = 9.61MW
COPh = 3.16
Technical paper