bali march 2015 - ineos · pdf filechlorine acrylonitrile maleic anhydride polyethylene...
TRANSCRIPT
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BICHLOR™ Electrolyser
Designed by Operators
for Operators
Dr Derek ArmstrongGlobal Sales and Marketing Manager
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4 PhD in Electrochemistry from Cambridge University
4 24 years experience in ICI/INEOS
4 Worked exclusively in the Chlorine Chain
� Chlor-alkali Electrolysers
� Electrode coatings
� EDC technology
� Perchlorethylene /Trichlorethylene
� Low Bromine Chlorine
� Chlorinated Paraffin
� Water treatment technology
4 Currently Global Sales and Marketing for INEOS Technologies Ltd
Speakers Profile
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INEOS
TURNOVER
$54BILLION
EMPLOYEES
17,000
PRODUCTION HERITAGE
AMOCO, BASF, BAYER, BOREALIS, BP, DEGUSSA, DOW, ENICHEM, ERDOLCHEMIE, HOECHST, ICI, INNOVENE, LANXESS, MONSANTO,NORSK HYDRO, SOLVAY
SITES
65 SITES IN 16
COUNTRIES
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50,000
1999200020012002200320042005200620072008200920102011201220132014
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INEOS GROWTH
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INEOS Technologies - licensing arm of INEOS
EDC/VCM/PVC
Chlorine Acrylonitrile
Maleic Anhydride
PolystyrenePolyethylene
Polypropylene
EMPLOYEES
450 +
HERITAGE
INEOS Technologies have expertise in:-
• Plant design
• Equipment design
• Process optimisation
• Catalyst selection & production
• Commissioning
• After sales support
• Extensive pilot plant facilities in USA, Europe & Asia
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INEOS Chlor alkali experience = 118 years
United Alkali Company
EVC
PVC(1986)
(1897)
chlor-alkali(1926)
chlor-alkali( 2001)
PVC/VCM/EDC(2001)
PVC/VCM/EDC(1986)
Stauffer
EDC/VCM(1989)
Cl2/EDC/VCM/PVC
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BiChlor - Global Presence
INEOS PROJECTS
More than 120 licensees world wide
Company Country kMTPA Start up
HF Chlor Alkali USA 110 2014
Skymine USA 90 2014
OLIN USA 200 2011
Company Country kMTPA Start up
Luzhou China 100 2009/13
Xinglong China 275 2011/12
Fuhua Tonga China 150 2009
Chengdu Chem China 105 2008/16
Wuhan China 100 2011
Company Country kMTPA Start up
Tasnim Bangaldesh 80 2011/15Company Country kMTPA Start up
Coogee Australia 50 2010/15
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BiChlor Electrolyser – Actual view
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BiChlor Electrolyser – Enhanced Attributes
• Zero Gap Technology
• Electrolyser output up to 50,000 MTPA per electrolyser
• Effective Area of modules 3.4 m2
• Normal operating current density 6.0 kA/m2
• Normal Operating Pressure range up to 300 mbarg
BiChlor electrolysers have the largest module area. This reduces the number of modules required per tonne NaOH
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• Modular
• Dimple Pan Design
• Short current path and uniform current distribution
• Electrode coatings
• Advanced Sealing
Looking inside the BiChlor electrolyser – Key Features
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INEOS Modular Design Enables:
• Fully Wetted Membrane• Gas/Liquor interface above the membrane
• Avoids damage and pin-holing of membrane
• Prevents mixing of Cl2 / H2 to avoid explosions
• Pressure testing before use (to detect and eliminate leaks)
• Maintenance work carried out away from the cell room• No risk of electrical shock
• Clean and safe work area
• No work carried out on top of the electrolyser
• Replacement modules can be prepared for rapid
electrolyser turn around
AnodeCathode Membrane
Gaskets
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Dimple pan design
• Reduced electrical resistance by
• Maximising use of nickel post in cathode pan
• Minimising use of titanium post in anode pan
• Strength
• Resistant to distortion during in-pan re-coating
• Resistant to pressure
• Self alignment of modules at commissioning
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Module construction showing dimples and “spider” structures
Cross Section through module
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Module construction showing dimples and “spider” structures
Current flow
• Each anode and cathode has hundreds of dimples
• Each dimple on the anode and cathode has a offset
distribution ‘spider’ attached to it
• Insulated pins redirect the current through the
spiders ‘legs’
Benefits
• Membrane fully supported no “flapping”
• Openness of contact points ensures even current
distribution with no “hot spots” and no localised
high concentration of product formation
• Prevents pinching of membrane
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Bichlor open mesh cathode structure
• BiChlor electrolysers have always used an open mesh cathode
• This provides the following advantages
• Enhanced catholyte circulation• Eliminates stagnation of catholyte
• This means no “hot spots” are generated and that all new high performance membranes can beused to optimise energy efficiency and reduce power consumption
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INEOS COATINGS
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KEY FACTS
INEOS manufactures all its own coatings
All INEOS coatings can be tailored to customers membrane cycles
Anodes – 8, 10, 12 years Cathodes – 8, 10, 12, 15, 16 years
INEOS coatings are currently installed in the following electrolysers• INEOS• UHDE• AK• MGC
INEOS HAS BEEN MANUFACTURING CHLOR ALKALI ELECTRODES FOR 118 YEARS
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INEOS Anode Coating – LOW CHLORINE OVER POTENTIAL
INEOS ANODE coatings have been designed to provide a chlorine over-
voltage of 20-30mV lower than typical commercial coatings. This represents a
1% power saving for customers (eg based on $80 per MWh a 100kte plant
would save $120k/year)
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40
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60
0 1 2 3 4 5 6 7 8
chlorine over-voltage (mV)
Time
Chlorine over-voltage
INEOS ANODE COATING
TYPICAL COMMERCIAL ANODE COATING
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INEOS Anode Coating – LOW ALKALINE WEAR
Accelerated Alkaline Wear Test - Voltage Rise - 20kA/m2 Current Density
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0 10 20 30 40 50 60 70 80 90 100 110 120 130 140
Duration (Hours)
Voltage ( V )
CP304 CompetitorINEOS
INEOS ANODE coatings have been designed to provide significantly superior alkaline
wear performance over other commercially available chlor-alkali anode coatings.
With the move to zero gap where the membrane lies directly up against the membrane
good alkaline wear resistance in very important for coating life as the surface of the
membrane is alkaline.
Time
StandardCommercialcoating
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INEOS Anode Coating – LOW CHLORATE IN BRINE
INEOS Competitor
Chlorate (g/l) 0.05 0.3
Hypochlorite (g/l) 0.8 1.5
INEOS ANODE coatings have been designed to provide a very low level of
chlorate (and hypochlorite) in brine.
This translates to less chemical usage for chlorate destruction but more
importantly lower chlorate in caustic, stopping evaporator corrosion.
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INEOS Cathode Coating – HIGH RESISTANCE TO WEAR
• Non-precious metal coatings normally last 4-8 years
• INEOS precious metal coating shows virtually no loss (warrantied for 16 years)
• >18 years experience in our FM mono-polar technology
• 13 years experience on BICHLOR™ with no measurable loss
Cathode coating loading vs time on load - schematic
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100
0
time on load
% of starting catalyst remaining in
coating
Non-precious metal coating
INEOS precious metal coating
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The INEOS CATHODE Coating has an exceptionally high resistance to
reverse currents making it the ideal cathode coating for all zero gap
electrolysers.
Coating totally failed
-0.350
-0.300
-0.250
-0.200
-0.150
-0.100
-0.050
0.000
0 100 200 300 400 500 600 700 800
E(V) verus RHE
Test Cycles
Accelerated Cathode Durability Data85°C 32% NaOH (Data HF Resistance Corrected)
INEOS cathode coating Competitor cathode coating
INEOS Cathode Coating - HIGH RESISTANCE TO REVERSE CURRENTS
Non precious metal cathode coating
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Continued focus on performance
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Advanced Sealing
• Gasket structure evolved over > 25 years
• Constructed of EPDM rubber with PTFE protection at the interfaces with the electrolytes
• Designed to minimise anode flange crevice corrosion
• Profiled at point of contact with membrane
• Diminished risk of leakage of products
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As Operators what are we looking for?
SuccessfulLifespan
SafeOperation
Reliability Efficiency
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With BiChlor you benefit from
• Safe Operation
• Designed for safety • Easy access to electrolyser components, e.g. headers• Module maintenance away from the electrolyser area• Module design prohibits chlorine and hydrogen explosions
• Reliability• Proven electrolyser design• Membranes guaranteed for 4 years minimum• Anode and cathode life up to 16 years • Performance backed up by product volume guarantees• Engineering and Technical back up help from INEOS team• Access to INEOS Technical service team at start up and whilst in production
• Efficiency • Leading position on power consumption• Performance backed up by product quality guarantees
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Plus: Our Commissioning and Technical Service offering
• Extensive commissioning support• Lead commissioning manager plus support as required
• Operator training
• Overview of frame and module build
• Electrolyser start-up
• Technical service support is part of the deal• No extra cost for standard level of support
• Designated Technical Service Manager
• Your link to our full technical team
• Regular contact• Visits at least once per year
• Phone & e-mail
• Performance evaluation and operating advice
• Technical support
• Electrolyser maintenance planning
• Customer forum every 2 years – highly valued by our clients
This document is the property of INEOS Technologies (Vinyls) Limited and the information it contains is strictly confidential and may not be copied, used or disclosed without the express permission of Ineos Technologies (Vinyls) Limited.27
INEOS will Bring Deep Understanding of Chlor-Alkali to your Project
• Design of wider chlor-alkali plant, whether for a technology conversion or new installation is by now generally understood
• Deep understanding of the chemical engineering science around the electrolysis section of the plant is required to ensure optimal design
• Several key areas, identified here, require very careful consideration to ensure prolonged efficient operation of the plant
• Operating Experience + Technical Expertise � Optimal Cellroom design
ContractorsINEOS
Client
Strengths Knowledge
CommunicateOptimise
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Where can INEOS add value?
Optioneering and financial analysis
Hazard studies and technical risk
Vendor analysis and selection
Dynamic modelling
Plant performance assessment
Process Definition
Process Design
Detailed Engineering
Commissioning
Procurement and Construction
Front End Engineering Expert processengineering
Operating skillsTechnology knowledge
Layout analysis
Feasibility studiesPlant capacity assessment
Troubleshooting
SIL/LOPA
PDPs
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In summary
• INEOS can provide the skills, knowhow and equipment to help
build and operate a successful plant
• Support to project feasibility studies
• Supply of first class engineering services
• Supply of BICHLOR™ Electrolysers
• Continued after sales support
JOIN THE INEOS FAMILY – “by operators for operators”
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