Technoeconomic Evaluation of MEA versus Mixed Amines for CO2 Removal at Near-Commercial Scale at Duke Energy Gibson 3 Plant

Jones, Dale A.; McVey, Thomas; Friedmann, S. Julio

doi:10.2172/1059463

Cited by 4 publications

(2 citation statements)

References 6 publications

Supporting

Mentioning

Contrasting

Order By: Relevance

“…, where q h GT , q c GT , w el GT are the specific heating, cooling, and electricity required per unit volume of amine, assumed to be constant and equal to, 31 respectively, 0.27 MJ/kg, 0.40 MJ/kg, and 46.5 kWh/kg.…”

Section: Scrmentioning

confidence: 99%

Techno-Economic Analysis of the Production of Liquid Biofuels from Sewage Sludge via Hydrothermal Liquefaction

et al. 2022

View full text Add to dashboard Cite

This work addresses the process and economic performance of the production of gasoline and diesel range fuels from urban sewage sludge. The overall production route involves direct conversion of the sewage sludge to an intermediate oil phase, so-called biocrude, via hydrothermal liquefaction at near-critical water conditions and further upgrading of the biocrude based on conventional refinery processes. The overall mass and energy yields of combined naphtha and middle distillate from sewage sludge on dry basis are approximately 19 and 60%, where the naphtha fraction represents about 45% of the total, with a minimum fuel selling price ranging between 2.4 and 0.8 €/liter assuming full investment in both the biocrude production and upgrading plant with sewage sludge feed capacities in the range of 3 to 30 dry-ton/day. If existing equipment at refinery can be used for upgrading of the biocrude, the minimum fuel selling price can be reduced by approximately 7%.

show abstract

Section: Scrmentioning

confidence: 99%

Techno-Economic Analysis of the Production of Liquid Biofuels from Sewage Sludge via Hydrothermal Liquefaction

et al. 2022

View full text Add to dashboard Cite

show abstract

“…For a more complete description of the project, consult the original Technoeconomic Evaluation. 17 We modeled the process using Aspen Plus, Version 7.0 without Rate-Based Distillation. Therefore, our model will calculate the results of the absorption and stripping columns assuming all species and phases are in equilibrium at each stage.…”

Section: Background and Scopementioning

confidence: 99%

Description of the Process Model for the Technoeconomic Evaluation of MEA versus Mixed Amines for Carbon Dioxide Removal from Stack Gas

Jones¹

2013

View full text Add to dashboard Cite

Facilitating CCS Business Planning by Extending the Functionality of the SimCCS Integrated System Model

Ellett¹,

Middleton

Stauffer

et al. 2017

Energy Procedia

View full text Add to dashboard Cite

Technoeconomic Evaluation of MEA versus Mixed Amines for CO2 Removal at Near-Commercial Scale at Duke Energy Gibson 3 Plant

Cited by 4 publications

References 6 publications

Techno-Economic Analysis of the Production of Liquid Biofuels from Sewage Sludge via Hydrothermal Liquefaction

Techno-Economic Analysis of the Production of Liquid Biofuels from Sewage Sludge via Hydrothermal Liquefaction

Description of the Process Model for the Technoeconomic Evaluation of MEA versus Mixed Amines for Carbon Dioxide Removal from Stack Gas

Facilitating CCS Business Planning by Extending the Functionality of the SimCCS Integrated System Model

Contact Info

Product

Resources

About