greenhydrogen installation considerations
TRANSCRIPT
GREEN HYDROGEN INSTALLATION
CONSIDERATIONS
Presented at GSTC Fall Meeting in San Antonio, TXOctober 11, 2021
byDominic M Varraveto & Chris Ploetz
Agenda
► Introduction & Background• Hydrogen Characteristics: Colors, Safety etc• Experience Integrating Hydrogen Plants• Hydrogen Technology Color Evolution
► Installing Green Hydrogen • Process Description• Basis: Setting the boundary between ISBL & BOP• Input Streams : Feedstock(s), Energy, Utilities• Output Flows: Product(s), By-products, Waste • Infrastructure: Connecting all the Pieces & Auxiliary Systems and • Project Experience
Question: What Color is your Hydrogen? Answer: It depends!
Hydrogen is the smallest and lease dense of all known molecules. At ambient conditions it is a colorless, diatomic gas that burns with a nearly invisible flame.
The color spectrum of visible light has recently been used to classify hydrogen by origin and reaction pathway.
However, hydrogen safety is colorblind and must account for extreme physical properties:
• Gas S.G.= 0.0696• Liquid Density = 4.423 lb/ft3• Boiling Point = -423 deg F• Flammability Range: 4 to 75 % by vol• Transport Fuel Pressure Range: 12k-15k psi
Hydrogen Spectrum
A quantitative alternative to colors is Carbon Intensity or CI, score: amount of CO2attributable to gathering, processing and consuming a fuel per energy released in g/MJ
SMR/Gray Hydrogen Experience
Client Location Project Name Technology
CVR WynnewoodMSAT 2 (included new Hydrogen plant) HydroChem
CVR Coffeyville New Hydrogen Project CB&I
Phillips 66 Billings VIP, Plant #1 Expansion UOP
Phillips 66 BorgerCoker & VDU Revamp (Hydrogen plant) Howe Baker
Phillips 66 Ponca CityULSD (included new Hydrogen plant) Howe Baker
Phillips 66 Ponca CityULSG (included new Hydrogen plant) Howe Baker
Phillips 66 Ponca CityGasoline Benzene Reduction (PSA) UOP
Praxair La Porte PSA Upgrade/Tailgas Compressor UOP
Praxair Plaquemine New PSA Unit UOP
Praxair Texas City 3rd Hydrogen Compressor Linde
Valero Memphis New Hydrogen Plant Technip
Valero McKee New Hydrogen Plant Technip
Hydrogen Installations Considerations
• Integration
• Intermittency
• Infrastructure
• Incentives
SMR/Gray Hydrogen Plant Integration Experience
Qualifications
Burns & McDonnell has extensive experience engineering and constructing “brownfield” SMR Hydrogen plants for existing refineries and Industrial hydrogen suppliers
Hydrogen Technology Color Evolution
Color Origin Pathway/Process Certified CI score1
Gray Hydrocarbon Naphtha, Nat Gas & Steam
Catalytic reforming
150-1662
Blue Nat Gas & Steam
Catalytic reforming w/CCUS
NA ?
Green Water Electrolysis 0.0
1. California Air Resource Board - LCFS Pathway Certified Carbon Intensities2. Includes logistics to compress, liquify and transport feed and product
INSTALLINGGREEN HYDROGEN
Process Description - Electrolysis► Chemistry
• 2H2O + Electricity à 2H2 + O2
§ Requires significant electrical input to drive the reaction
► Types• Alkaline
§ Lower cost at scale§ Well established technology
• Proton Exchange Membrane§ Faster ramp rates§ Less auxiliary equipment§ No Caustic Solution
• Solid Oxide§ Developing technology§ High efficiency
PEM ElectrolysisUS Dept of Energy
Alkaline ElectrolysisKamaroddin, et al
Solid OxideEnergy.nl
Inputs
US National Renewable Energy Laboratory
► Renewable Electricity• Green Hydrogen requires 100% Renewable
Electricity§ Electrolyzer H2 from Grid Energy has
higher CI than typical SMR (gray)• Electricity consumption is high
§ 10 MW Train à 2 MMSCFD H2
• What to do when not available?§ Energy Storage § Hydrogen Storage
► Water• High quality water required
§ Better than BFW• Typically RO required
Renewable Electricity - Availability
► Renewable Electricity can be highly variable• Especially true if onsite wind / solar
► If Green H2 consumption is continuous• Energy Storage
§ Can be offsite by utility• H2 Storage
§ Double or triple electrolyzer capacity and add H2 storage
► Consider if combo solution is feasible• Green H2 / Gray H2 mix has lower CI than
Electrolysis H2 from Grid Average Electricity
US National Renewable Energy Laboratory
US National Renewable Energy Laboratory
Outputs► Products
• Green Hydrogen§ PEM: 99.999%+ purity§ Alkaline: 99.9%+ purity,
– Additional purification to reach 99.999% purity§ Both may require downstream dehydration depending on application (e.g., vehicle fueling)
► Byproducts • Oxygen
§ 99.5% purity§ Consider if potential for use onsite
– E.G., oil refinery FCC or sulfur plant► Waste
• RO reject water• Spent caustic solution (alkaline)
► Reject Heat
Auxiliary Systems
Electrolyzer
Cooling
Water Treatment
Wastewater Treatment
H2 Compression?H2 Liquefaction?
H2 Storage?
Renewable Electricity Power Storage?
H2 Consumption
Auxiliary Systems - Summary► Electrical Infrastructure
• Onsite vs Purchased Renewable Energy• Energy Storage
§ Battery or Supercapacitor► Water Treatment
• If starting from city water, expect ~40% reject• Feedwater impurities (TDS/TSS) accumulate in the stack, so need to be minimized
► Cooling• Up to ~40% of the rated power is rejected as heat
► Compression• To storage pressure or usage pressure• GH2 storage pressure is typically high: ~6,500 psig• GH2 vehicle fueling is 10,000 – 15,000 psig
► Liquefaction► Storage
Project Experience – Gas Utility
► 0.4 MMSCFD Green Hydrogen► 2.5 MW Containerized PEM
• Continuous H2 Consumption§ Electrolyzer operates ~80% of
the time to avoid peak hours§ Requires H2 Storage
• Consumed as § NG fuel blendstock§ Fleet car fueling
• Packaged with Water Treatment and Cooling systems
► 2.5 MW of Green Electricity• Offsite generation
Project Experience – Refinery SMR Alternative
►10 MMSCFD Green Hydrogen►~5 x 10 MW Trains
• Requires continuous H2 production• Centralized Water Treatment and
Cooling systems►~55 MW of Green Electricity
• Offsite generation• Challenging infrastructure and
procurement problem
Q & A