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Pyrolysis of municipal solid waste with iron-based additives: A study on the kinetic, product distribution and catalytic mechanisms

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TLDR
In this paper, the effects of two iron-based additives (iron ore and iron oxide) on the pyrolysis characteristics of municipal solid waste (MSW) were investigated by using TGA, and the kinetic results illustrated that the average activation energy was 180.32 kJ/mol, while the reduction of iron ore and the catalytic mechanism were analyzed by H2-TPR, XPS and BET.
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This article is published in Journal of Cleaner Production.The article was published on 2020-06-10. It has received 137 citations till now. The article focuses on the topics: Iron oxide & Iron ore.

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Melting process of nanoparticle enhanced PCM through storage cylinder incorporating fins

TL;DR: In this paper, the authors discuss how the arrangement of fins can affect the charging process and how to find the optimized style of fin to gain the highest performance by using fins over both inner and outer pipes.
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Approaches for expedition of discharging of PCM involving nanoparticles and radial fins

TL;DR: In this paper, a sinusoidal tank including inner circular cylinder was considered and to expedite the solidification, radial fins were installed over the inner cold cylinder to improve the conduction, CuO nano sized material was added and effects of size of particles were involved.
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Plastic waste upcycling toward a circular economy

TL;DR: In this article, a review of the current advances and future directions in plastic waste upcycling technologies are discussed, focusing on the production of high-value materials from plastic waste conversion methods, including pyrolysis, gasification, photoreforming, and mechanical reprocessing.
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Gasification of municipal solid waste blends with biomass for energy production and resources recovery: Current status, hybrid technologies and innovative prospects

TL;DR: In this article, the current status of utilization of municipal solid waste and biomass blends for energy and resources recovery together with identifying the opportunities for future development in technological equipment and physicochemical waste compositions involved in such complex processes.
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Nanoparticles for phase change process of water utilizing FEM

TL;DR: In this article, the authors presented the needed time values for full solidification with impose of fins and various sizes of nanoparticles, contours and solid front configurations were depicted in outputs obtained from (Finite element method) FEM modeling.
References
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Journal ArticleDOI

Application of response surface methodology in describing the performance of coated carbide tools when turning AISI 1045 steel

TL;DR: In this article, the performance of a multilayer tungsten carbide tool was described using response surface methodology (RSM) when turning AISI 1045 steel.
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Pyrolysis of waste tyres: a review.

TL;DR: Examples of commercial and semi-commercial scale tyre pyrolysis systems show that small scale batch reactors and continuous rotary kiln reactors have been developed to commercial scale.
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Cooperativity and Dynamics Increase the Performance of NiFe Dry Reforming Catalysts

TL;DR: Owing to the high activity of the material and the absence of any XRD signature of FeO, it is very likely that FeO is formed as small domains of a few atom layer thickness covering a fraction of the surface of the Ni-rich particles, ensuring a close proximity of the carbon removal (FeO) and methane activation (Ni).
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Toxicity of leachate from weathering plastics: An exploratory screening study with Nitocra spinipes.

TL;DR: An initial screening of the marine environmental hazard properties of leachates from weathering plastics to the marine harpacticoid copepod [Crustacea] Nitocra spinipes demonstrates that leachate from different plastics differ in toxicity to N. spinipes and that the toxicity varies under simulated weathering.
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Fast pyrolysis of biomass and waste plastic in a fluidized bed reactor

TL;DR: In this article, a co-pyrolysis of red oak and high density polyethylene (HDPE) was conducted in a laboratory-scale, continuous fluidized bed reactor in a temperature range from 525 to 675°C.
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