Search results for: “reforming”
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Methane reforming: costs of grey hydrogen, costs of blue hydrogen?
This data-file captures the economics of blue hydrogen production via reforming natural gas: either steam-methane reforming or auto-thermal reforming. Costs and operating parameters are compiled from technical papers. Blue hydrogen can be cost-competitive with CCS, while overall costs are most sensitive to gas prices.
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Topsoe: autothermal reforming technology?
Topsoe autothermal reforming technology aims to maximize the uptime and reliability of blue hydrogen production, despite ultra-high combustion temperatures from the partial oxidation reaction, while achieving high energy efficiency, 90-97% CO2 capture and
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Blue ammonia projects: a screen?
This data-file captures a sample of 30MTpa of blue ammonia projects from 1980 to 2030, including their location, companies, timings (year of FID, year of start-up), their sizes (in MTpa), their CO2 reductions (in %), their capex costs (in $M, where disclosed) and the implied capex costs ($/Tpa). We have also summarized each project with…
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US hydrogen production: by facility and by company?
10MTpa of hydrogen is produced in the US, of which 40% is sold by industrial gas companies, 20-25% is generated on site at refineries, 20% at ammonia plants and 15-20% in chemicals/methanol. This datafile breaks down US hydrogen production by facility. Owners of existing steam methane reforming units may readily be able to capture CO2…
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Energy needed to produce steam: enthalpy and entropy data?
This data-file quantifies the energy needed to produce steam, for industrial heat, chemicals, CCS plants and hydrogen reforming? As rules of thumb, low pressure saturated steam at 100◦C requires 2.6 GJ/ton (720kWh/ton), medium pressure dry steam at 6-bar and 300◦C requires 3 GJ/ton (830kWh/ton) and super-critical steam at 250-bar and 600◦C requires 4 GJ/ton (1,150kWh/ton).
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Pressure swing adsorption: energy economics?
Pressure swing adsorption purifies gases according to their differing tendencies to adsorb onto adsorbents under pressure. Pressure swing adsorption costs $0.1/kg when separating pure hydrogen from reformers, and $2-3/mcf when separating bio-methane from biogas. Our cost breakdowns include capex, opex, maintenance, zeolite replacement, compression power and CO2 costs.
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Hydrogen reformers: SMR versus ATR?
Blue hydrogen value chains are gaining momentum. Especially in the US. So this 16-page note contrasts steam-methane reforming (SMR) versus autothermal reforming (ATR). Each has merits and challenges. ATR looks excellent for clean ammonia. While the IRA creates CCS upside for today’s SMR incumbents, across industrial gases, refining and chemicals.
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Polyester: production process?
Polyester is the most produced textile fiber on planet Earth. Of the world’s 8GTpa of oil and gas production, 80MTpa, or 1% ends up as PET, via eleven chemical processing stages that span naphtha-reforming, BTX separation into paraxylene, oxidation to PTA, plus ethane cracking, ethylene oxide and ethylene glycol. This data file covers the polyester…
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Global PGM demand: breakdown by metal and use?
Core global PGM demand ran at 565 tons in 2023, which remains c6% lower than the all-time peak demand of 600Tpa in 2019. We model a recovery to 700 Tpa of demand for platinum, palladium and rhodium in 2030, then a long run decline to 350Tpa if EVs ultimately reach 90% of vehicle sales by…
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Global plastic demand: breakdown by product, region and use?
Global plastic is estimated at 470MTpa in 2022, rising to at least 800MTpa by 2050. This data-file is a breakdown of global plastic demand, by product, by region and by end use, with historical data back to 1990 and our forecasts out to 2050. Our top conclusions for plastic in the energy transition are summarized.
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