2021
DOI: 10.1016/j.jcou.2021.101436
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Alternative carbon dioxide utilization in dimethyl carbonate synthesis and comparison with current technologies

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Cited by 20 publications
(12 citation statements)
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“…23 Finally, in the third phase, we use the ReCiPe v1.1 methodology to calculate the life cycle impact assessment (LCIA) from the LCIs again using Brightway2 v2.4.2. 28 Economic Assessment. The production cost per kg of VCM is calculated based on the raw material and utility consumption of the plant, assuming that the effect of the capital cost is negligible due to economies of scale (Section D of the Supporting Information) and the high operating costs eqs 1 and 2, as it was found in other petrochemical processes 29−31 (1)…”
Section: ■ Methodologymentioning
confidence: 99%
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“…23 Finally, in the third phase, we use the ReCiPe v1.1 methodology to calculate the life cycle impact assessment (LCIA) from the LCIs again using Brightway2 v2.4.2. 28 Economic Assessment. The production cost per kg of VCM is calculated based on the raw material and utility consumption of the plant, assuming that the effect of the capital cost is negligible due to economies of scale (Section D of the Supporting Information) and the high operating costs eqs 1 and 2, as it was found in other petrochemical processes 29−31 (1)…”
Section: ■ Methodologymentioning
confidence: 99%
“…The production cost per kg of VCM is calculated based on the raw material and utility consumption of the plant, assuming that the effect of the capital cost is negligible due to economies of scale (Section D of the Supporting Information) and the high operating costs eqs and , as it was found in other petrochemical processes C var = j J F j feed · cost j feed + u U Q u · cost u utility cos normalt VCM = C var F VCM product where C var is the variable operating cost of the plant [$ h –1 ]; J is the set of raw materials ( i.e. , mass inputs) involved in the synthesis of VCM; F j feed is the mass flow [kg h –1 ] of raw material j ; U is the set of utilities required for the synthesis of VCM, including heating, cooling at 20 to 25 °C, refrigeration at −50 °C, refrigeration at −125 °C, and electricity; Q u is the energy flow [MW] of utility u ; cost j feed and cost u utility are the prices of raw material j [$ h –1 ] and utility u [$ MW –1 ], respectively; F VCM product is the mass flow [kg h –1 ] of the product; and cost vcm is the production cost of VCM [$ kg –1 ].…”
Section: Methodsmentioning
confidence: 99%
“…With the acceleration of industrialization worldwide, using petroleum resources to synthesize materials emits a large amount of carbon dioxide (CO 2 ), which has aroused people’s attention to environmental warming. How to use sustainable resources to develop high-performance and environmentally friendly materials has become a global issue. Faced with this situation, the direct use of CO 2 to prepare chemical monomers or polymers has been further studied.…”
Section: Introductionmentioning
confidence: 99%
“…[1,2] Among which, the conversion of CO 2 into dimethyl carbonate (DMC) was a favorable route to utilize CO 2 , because this route had high atomic efficiency and was environmentally friendly. [3,4] In addition, the product DMC has broad application prospects in the industrial field owing to its excellent chemical properties and high versatilities. [5] However, the negligible reactivity of CO 2 and the thermodynamic equilibrium limitation of this reaction making the route full of challenge.…”
Section: Introductionmentioning
confidence: 99%