A conceptual evaluation of a new multifunctional reactor containing glycerol steam reforming and nitrobenzene hydrogenation

Continuous Fatty Acid Production: Comparative Technoeconomic and Life-Cycle Analysis between Subcritical Water and Lipase Methods

“…In this work, palmitic acid is the main product, while crude glycerol is considered as a byproduct. The selling price of crude glycerol is assumed to be 170 USD/ton . The equipment’s depreciation is estimated via a straight-line depreciation method over the plant’s life span (20 years).…”

“…The selling price of crude glycerol is assumed to be 170 USD/ton. 31 The equipment's depreciation is estimated via a straight-line depreciation method over the plant's life span (20 years). The income tax is assumed to be 30%.…”

Technical, economic, and environmental potential of glycerol hydrogenolysis: a roadmap towards sustainable green chemistry future

“…41 (b) Optimization of the reactor and PSA unit design to further increase efficiency and reduce costs, adopting intensi-cation techniques (i.e., semi-batch reactors, low-pressure PSA, and utilization of ue gas as a source of power). 42,43 (c) Investigation of the potential use of highly stable catalysts for both glycerol reforming and hydrogenolysis reactions to improve the yield of 1,2-PDO and glycerol conversion up to ca. 90%.…”

Multi-objective optimization of aniline and hydrogen production in a directly coupled membrane reactor

“…NBH is the main method for aniline production [47]. Aniline is mainly used as a precursor of polyurethane and has a worldwide market in 2020 of 6.2 million tons [48]. The NBH reaction is:…”