2020
DOI: 10.1016/j.joule.2020.09.006
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Process Intensification through Directly Coupled Autothermal Operation of Chemical Reactors

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Cited by 33 publications
(34 citation statements)
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References 68 publications
(82 reference statements)
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“…Fiaschi et al 106 demonstrated a 180% increase in the recovery of heat from the exhaust of an industrial textile drying process through redesign of the heat exchanger network by employing improved computational design methods including multi-scale, multi-physics CFD (computational fluid dynamics), and a recent perspective in these pages identified opportunities for autothermal operation of chemical reactors through direct coupling of endo-and exothermic processes. 107 At the system level, opportunities exist to integrate industrial parks for better overall utilization of waste heat and material flows 108 and into broader district heating systems where low-value waste heat can be employed for space heating of buildings. 109 These applications are generally limited by the fact that heat transport is most readily accomplished using steam distribution systems, which limits both the temperature range of the industrial park thermal distribution system and the distance it can travel.…”
Section: Less Loss With Better Insulationmentioning
confidence: 99%
“…Fiaschi et al 106 demonstrated a 180% increase in the recovery of heat from the exhaust of an industrial textile drying process through redesign of the heat exchanger network by employing improved computational design methods including multi-scale, multi-physics CFD (computational fluid dynamics), and a recent perspective in these pages identified opportunities for autothermal operation of chemical reactors through direct coupling of endo-and exothermic processes. 107 At the system level, opportunities exist to integrate industrial parks for better overall utilization of waste heat and material flows 108 and into broader district heating systems where low-value waste heat can be employed for space heating of buildings. 109 These applications are generally limited by the fact that heat transport is most readily accomplished using steam distribution systems, which limits both the temperature range of the industrial park thermal distribution system and the distance it can travel.…”
Section: Less Loss With Better Insulationmentioning
confidence: 99%
“…With the introduction of a larger excess of water, the formed hemihydrate undergoes full hydrolysis at the second stage. This process occurs quickly and is accompanied by the release of gaseous acetylene and the precipitation of calcium hydroxide (3). In this case, DMSO molecules are released from a coordinated state into a solution.…”
Section: Optimization Of the Heat Release Profilementioning
confidence: 99%
“…Many attempts have been made to combine exo- and endothermic processes. As a result, autothermal reaction setups were developed [ 3 ]. However, the scope of autothermal reactions is limited.…”
Section: Introductionmentioning
confidence: 99%
“…Although chemical kinetics would ideally set the maximum rate that pyrolysis proceeds in a reactor, the transport of heat into the reactor more likely determines this rate. In a recent perspective paper on directly coupled autothermal operation of chemical reactors, we showed that the maximum diameter of a tubular reactor to avoid heat transfer becoming the bottleneck to processing rates is given by where h (kJ s –1 m –2 K –1 ) is the heat transfer coefficient, Δ T (K) is the temperature gradient across the wall of the reactor, k pyr (s –1 ) is the reaction rate coefficient for an assumed first-order pyrolysis reaction, C A (kg m –3 ) is the concentration of the reactant, and Δ H r,pyr (kJ kg –1 ) is the enthalpy change for the pyrolysis reaction. For pyrolysis in a fluidized bed, appropriate values of h and Δ T are 0.1 kJ s –1 m –2 K –1 and 400 K, respectively, k pyr and C A equal 0.094 s –1 and 180 kg m –3 , respectively, and Δ H r,pyr is equal to 1000 kJ kg –1 .…”
Section: Autothermal Pyrolysismentioning
confidence: 99%
“… a L , reactor length; A S /tube, surface area of a heat transfer tube in the reactor; tubes/ A C , number of tubes per cross-sectional area of the reactor; j p , mass flux of the granular heat carrier entering the reactor; C p Δ T , sensible energy per unit mass of the granular heat carrier. This scheme was reproduced with permission from ref . Copyright 2020 Elsevier. …”
Section: Autothermal Pyrolysismentioning
confidence: 99%