Methane Cracking CMAT Energy Solutions

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Presentation transcript:

Methane Cracking CMAT Energy Solutions Andrew Lipe, Matt Paintner, Tyler Webber, Caleb Weddle

Purpose Producing high purity Hydrogen from Methane (Natural Gas) with low CO2 emissions Current process: Steam Reforming of Methane Proven Technology Industry Standard Relatively Inexpensive Produces significant amounts of CO2  (~ 8 ton/ton H2) Requires large quantities of water

Preferred Process Hydrogen Production via Direct Contact Pyrolysis of Natural Gas Temperatures of 1500⁰F to 1700⁰F  Pressure ranging from 40 psia to 70 psia   Methane conversions of 95% and higher CH4(g) -> C(s) + 2H2(g)     ΔH = 75 kJ/mol Requires no water for reaction to occur Produces CO2 emissions from firing furnace, not from actual process  Feedstock readily available

Business Opportunity Feedstock Cost Product Price Byproduct Price Uses for Hydrogen  Ammonia Synthesis   Synthesis of Methanol and Cyclohexane   Removal of Sulfur from fuels during oil-refining  Uses for Graphite Used in steel manufacturing to coat foundry molds Manufacturing of brakes, brake linings, clutch facings, friction components and mechanical seals Industrial lubricants and metal powders Feedstock Cost   Industrial Natural Gas: $3.28/Mcuft  Product Price   Hydrogen: $0.31/lb   Byproduct Price   Graphite: $0.45/lb 

Sizing and Location Plant Size Location 100 million lb/yr H2 produced Gulf Coast Many refineries in a central location Port Arthur, Texas offers a central location near a major refinery and is located close to the coast

Furnace Utilize Heat from furnace as much as possible Heat molten tin to be used as heat transfer fluid in closed loop system Create steam to supply electricity to necessary components of the process Generate steam to trace the lines that transfer the tin heat transfer fluid to prevent build up Preheat air being fed to the furnace burners

Reactors 1 reactor necessary for continuous process Reactor Size Overflow system used  Carbon will continuously overflow and be taken out of the reactor Reactor Size Diameter: 12 ft Height: 52 ft Reactor building material 316 Stainless Steel Silica firebrick to help withstand extreme conditions Mott Corporation porous metal filters to increase heat transfer area Insulation  Reactors will be insulated to prevent as much heat loss as possible

Carbon Separation Carbon will build up in reactor until it reaches an overflow port. This port will funnel the carbon to a cyclone separator. Vapor flow from the reactor will serve as driving force to ensure carbon reaches the cyclone. Once in the separator, carbon will settle and vapor will exit out of the top of the cyclone. The carbon will fall from the cyclone into a water deluge rotary cooler to be cooled and then transported off site or to storage.

Simulation

Safety High explosion hazard High temperature of reactor Due to temperatures being above auto ignition for carbon flakes and hydrogen Must be an oxygen free environment  High temperature of reactor Personal Protective Equipment (PPE) needed for personnel Proper control systems needed to maintain stability  Corrosion and embrittlement High temperatures of tin and hydrogen can cause possible risks of corrosion and embrittlement

Environmental Carbon Dioxide Carbon Monoxide NOx 197,432.47 tons/yr --- .03% of Texas overall CO2 production. No EPA regulations exist for industries yet 1.97 tons/ton Hydrogen Carbon Monoxide 21.86 tons per year. --- 4.99 pounds per hour EPA regulation 9 ppm per 8 hours NOx 1003.22 tons per year  ---  228.89 pounds per hour EPA regulation .08 pounds of NOx /MMBtu (furnace) Control methods- SNCR and SCR

Economic Analysis FCI: $111 million Revenue: $165 million/yr TCI: $130 million NPV0: $1.82 billion NPV10: $686 million IRR: 50%

Final Recommendations Perform process on lab scale followed by intermediate scale to verify conversions, design integrity, safety and overall performance. Further verify that overflow system and carbon removal steps will perform adequately. Attain specific quotes on equipment using operating conditions and dimensions. Further analysis on global impact of producing such a high amount of graphite.

Questions?