Point Source Carbon Capture from Industrial Sources

CO₂ Capture from Ethanol Facilities | CO₂ Capture from Iron and Steel Production | CO₂ Capture from Cement Plants | CO₂ Capture from Hydrogen Production

Point source carbon capture from industrial sources (e.g., chemical production [ammonia, hydrogen, petrochemical], mineral production [cement and lime], natural gas processing, and iron and steel production plants) separates carbon dioxide (CO₂) emissions from the plant’s flue gas or other exhaust stream that would otherwise have been released to the atmosphere. As the U.S. industrial sector accounted for over 1,300 million tonnes of CO₂ emissions in 2020^[i], the deployment of point source capture technologies from industrial sources is a vital element in reducing CO₂ emissions.

The U.S. Department of Energy/National Energy Technology Laboratory’s (DOE/NETL) Point Source Carbon Capture Program is supporting engineering-scale testing and front-end engineering design (FEED) studies on carbon capture technologies that separate at least 95% of the total CO₂ emissions at industrial facilities. Furthermore, NETL is addressing challenges with the application of carbon capture, utilization and storage (CCUS) to steam methane reforming (SMR) and autothermal (ATR) plants, such as increased levelized cost of hydrogen at high carbon capture rates, increased natural gas consumption, and/or reduced amounts of electricity, through initial engineering designs of commercial-scale, advanced CCUS systems that separate and store or utilize CO₂, with 90% carbon capture efficiency, from SMR or ATR plants producing high-purity hydrogen from natural gas. The complexity of capturing CO₂ from industrial sources varies across the sector with CO₂ concentrations greatly depending on the industry and the specific stream targeted for CO₂ capture. Industrial sources that have a highly concentrated stream of CO₂, such as natural gas processing, fertilizer production, hydrogen production, and ethanol production, have lower energy requirements for CO₂ separation. For lower-concentration industrial sources, such as iron and steel production, cement manufacturing, and petroleum refining facilities, significant challenges exist in developing carbon capture technologies, including energy requirements, differing gas compositions, varying process temperatures and pressures, and various contaminants.

Archer Daniels Midland’s Agricultural Processing and Biofuels Plant in Decatur, Illinois; CO₂ Capture from Biofuels Production and Storage into the Mt. Simon Sandstone.

Red Trail Energy’s ethanol plant in Richardton, North Dakota.

CO₂ Capture from Iron and Steel Production

Schematic of solvent-based carbon capture from blast furnace-based steel plant.

Primary steel production typically uses iron ore and the process known as blast furnace with basic oxygen furnace (BF-BOF). For BF-BOF steel plants, capture technologies target CO₂ from the blast furnace gas as it contains the highest CO₂ concentration by volume within the steelmaking process. Various process heaters located throughout the plant account for a large amount of CO₂ emissions; however, carbon capture from these is difficult without a common flue stack.

CO₂ Capture from Hydrogen Production

Schematic of hydrogen production via steam methane reforming with various CO₂ capture options.

Schematic of hydrogen production via autothermal reforming with CO₂ capture.

Hydrogen production via steam methane reforming (SMR) involves reacting natural gas and steam to produce synthesis gas (syngas), a mixture of carbon monoxide and hydrogen gas. A water-gas shift reaction may be performed to increase the amount of hydrogen gas in the product gas which also increases the concentration of CO₂ in the shifted syngas. Hydrogen production emits CO₂ from the process gas and from the combustion of natural gas (flue gas). When producing hydrogen via SMR, there are three separate point sources in which CO₂ can be collected or vented from the plant: from the SMR flue gas, from the syngas stream before pressure swing adsorption (PSA), and from the PSA tail gas. In autothermal reforming (ATR) plants, either highly pure oxygen from an air separation unit (ASU) or input air is added to partially oxidize the natural gas, producing hydrogen-rich syngas. The autothermal (internal) combustion process in ATR plants results in a higher concentration of CO₂ in the syngas than in the flue gas.  Since CO₂ capture from flue gas is considerably more expensive and complex (low CO₂ partial pressure, N₂/O₂ impurities) than from syngas, it is more economical to capture the CO₂ from the syngas stream prior to entering the PSA unit in an ATR plant. 

Through a U.S. Department of Energy (DOE)-funded project led by Air Products and Chemicals, Inc., two SMR hydrogen production plants located within the Valero Refinery in Port Arthur, Texas were successfully retrofitted with vacuum swing adsorption systems to separate the CO₂ from the process gas stream. The process concentrates the CO₂ in the reformer process gas stream from 10-20% to greater than 97% CO₂ purity, while capturing more than 90% of the CO₂ in that stream^[iii].

Air Products and Chemicals Inc.’s refinery in Port Arthur, Texas.

[i] U.S. Energy Information Administration. U.S. Energy-Related Carbon Dioxide Emissions, Monthly Energy Review.  https://www.eia.gov/totalenergy/data/monthly/pdf/sec11.pdf

[ii] “Cost of Capturing CO₂ from Industrial Sources.” National Energy Technology Laboratory. January 10, 2014. ESPA Authoring Template (doe.gov)

[iii] “Air Products and Chemicals, Inc.: Demonstration of CO₂ Capture and Sequestration of Steam Methane Reforming Process Gas Used for Large-Scale Hydrogen Production.” National Energy Technology Laboratory. July 2017. https://www.netl.doe.gov/sites/default/files/netl-file/FE0002381.pdf