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  • image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Authors: Petar Sabev Varbanov; Stanislav Boldyryev;

    This paper deals with analysis of energy consumption of Ukrainian bromine plant. Process integration allows reducing the energy consumption on 1.5 MW by heat recovery. It is achieved by improvement of recuperative heat exchangers network. Additionally heat recovery may be increased by multistage evaporation of sodium bromide and ferrous chloride. Increase the heat recovery leads utility reduction. This is not only heating and cooling duty but also power pumping and pipe heat losses. The investment for retrofit project is about 757 100 € and payback period about 2 years.

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Chemical Engineering Transactions
    Article . 2014
    Data sources: DOAJ
    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    image/svg+xml Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao Closed Access logo, derived from PLoS Open Access logo. This version with transparent background. http://commons.wikimedia.org/wiki/File:Closed_Access_logo_transparent.svg Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao
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      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
      Chemical Engineering Transactions
      Article . 2014
      Data sources: DOAJ
      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
      image/svg+xml Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao Closed Access logo, derived from PLoS Open Access logo. This version with transparent background. http://commons.wikimedia.org/wiki/File:Closed_Access_logo_transparent.svg Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao
      addClaim

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  • image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Authors: Petar Sabev Varbanov; Stanislav Boldyryev;

    This paper deals with analysis of energy consumption of Ukrainian bromine plant. Process integration allows reducing the energy consumption on 1.5 MW by heat recovery. It is achieved by improvement of recuperative heat exchangers network. Additionally heat recovery may be increased by multistage evaporation of sodium bromide and ferrous chloride. Increase the heat recovery leads utility reduction. This is not only heating and cooling duty but also power pumping and pipe heat losses. The investment for retrofit project is about 757 100 € and payback period about 2 years.

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Chemical Engineering Transactions
    Article . 2014
    Data sources: DOAJ
    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    image/svg+xml Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao Closed Access logo, derived from PLoS Open Access logo. This version with transparent background. http://commons.wikimedia.org/wiki/File:Closed_Access_logo_transparent.svg Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao
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      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
      Chemical Engineering Transactions
      Article . 2014
      Data sources: DOAJ
      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
      image/svg+xml Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao Closed Access logo, derived from PLoS Open Access logo. This version with transparent background. http://commons.wikimedia.org/wiki/File:Closed_Access_logo_transparent.svg Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao
      addClaim

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  • image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Authors: Suoton Philip Peletiri; Iqbal M. Mujtaba; Nejat Rahmanian;

    With about 195 countries signing the Paris (climate) Agreement and world leaders uniting for the planet after the United States’ notification to pull out of the agreement, many carbon capture and storage (CCS) projects are expected to be executed worldwide. Captured CO2 is not pure and may contain several impurities, which affect the flow dynamics of the CO2 fluid in pipelines. To design efficient CO2 pipeline transportation systems, it is imperative to understand the effect of these impurities on the flow behaviour. Aspen HYSYS (V10) and HydraFlash were used to study the behaviour of 90 mol % CO2 and 10 mol % single impurity (N2, CH4, H2, H2S, SO2, Ar, CO, NH3, O2 and H2O). The Peng-Robinson equation of state (EoS), which has the lowest average absolute deviation (AAD) among cubic EoS for predicting CO2 fluid properties, was used in Aspen HYSYS. Three different 50 km pipelines were simulated; one horizontal pipeline and two pipelines with +300 and -300 m in elevation between inlet and outlet respectively. The mass flow rate is 266,400 kg/h and the internal and external diameters of the pipelines are 0.289 m and 0.324 m respectively. All impurities changed the parameters of the flowing fluid. H2 impurity caused the most pressure loss for horizontal pipelines but may cause the least pressure loss for pipelines at high inclination angles. H2 and H2S formed the widest and narrowest two-phase regions, respectively. The results also show that H2 impurity resulted in the most heat loss while H2O and SO2 impurities had the lowest heat losses. Pipeline elevation change also affects the effect of each impurity on pressure changes. The difference in pressure drop between the impurity with the highest effect, H2, and that with the least effect, SO2, is 0.44 MPa for inclined pipelines, 0.77 MPa for horizontal pipelines and 1.44 MPa for declined pipelines. H2S had the mildest effect followed by NH3, H2O, SO2, CO, Ar, CH4, O2, N2 and H2.

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Chemical Engineering Transactions
    Article . 2018
    Data sources: DOAJ
    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
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      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
      Chemical Engineering Transactions
      Article . 2018
      Data sources: DOAJ
      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
      addClaim

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  • image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Authors: Suoton Philip Peletiri; Iqbal M. Mujtaba; Nejat Rahmanian;

    With about 195 countries signing the Paris (climate) Agreement and world leaders uniting for the planet after the United States’ notification to pull out of the agreement, many carbon capture and storage (CCS) projects are expected to be executed worldwide. Captured CO2 is not pure and may contain several impurities, which affect the flow dynamics of the CO2 fluid in pipelines. To design efficient CO2 pipeline transportation systems, it is imperative to understand the effect of these impurities on the flow behaviour. Aspen HYSYS (V10) and HydraFlash were used to study the behaviour of 90 mol % CO2 and 10 mol % single impurity (N2, CH4, H2, H2S, SO2, Ar, CO, NH3, O2 and H2O). The Peng-Robinson equation of state (EoS), which has the lowest average absolute deviation (AAD) among cubic EoS for predicting CO2 fluid properties, was used in Aspen HYSYS. Three different 50 km pipelines were simulated; one horizontal pipeline and two pipelines with +300 and -300 m in elevation between inlet and outlet respectively. The mass flow rate is 266,400 kg/h and the internal and external diameters of the pipelines are 0.289 m and 0.324 m respectively. All impurities changed the parameters of the flowing fluid. H2 impurity caused the most pressure loss for horizontal pipelines but may cause the least pressure loss for pipelines at high inclination angles. H2 and H2S formed the widest and narrowest two-phase regions, respectively. The results also show that H2 impurity resulted in the most heat loss while H2O and SO2 impurities had the lowest heat losses. Pipeline elevation change also affects the effect of each impurity on pressure changes. The difference in pressure drop between the impurity with the highest effect, H2, and that with the least effect, SO2, is 0.44 MPa for inclined pipelines, 0.77 MPa for horizontal pipelines and 1.44 MPa for declined pipelines. H2S had the mildest effect followed by NH3, H2O, SO2, CO, Ar, CH4, O2, N2 and H2.

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Chemical Engineering Transactions
    Article . 2018
    Data sources: DOAJ
    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
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      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
      Chemical Engineering Transactions
      Article . 2018
      Data sources: DOAJ
      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
      addClaim

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  • image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Authors: G. Cantarelli Lopes; L. Machado Da Rosa; M. Mori; J.R. Nunhez; +1 Authors

    Abstract preview not available - see full-text PDF article.

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Chemical Engineering Transactions
    Article . 2011
    Data sources: DOAJ
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      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
      Chemical Engineering Transactions
      Article . 2011
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  • image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Authors: G. Cantarelli Lopes; L. Machado Da Rosa; M. Mori; J.R. Nunhez; +1 Authors

    Abstract preview not available - see full-text PDF article.

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Chemical Engineering Transactions
    Article . 2011
    Data sources: DOAJ
    addClaim

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      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
      Chemical Engineering Transactions
      Article . 2011
      Data sources: DOAJ
      addClaim

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  • image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Authors: Rui Feng; Rongrong Zhang;

    In the past decades, China has adopted a wide variety of policies to stimulate bioenergy development, playing a more significant role in China’s energy structure. However, bioenergy development in China is still at an early stage and lags far behind other foreign countries. This study is aimed to explore the reasons behind this sluggish development from a policy perspective. Bioenergy development potential and provincial geographic distribution were investigated in China, which shows that the total technical bioenergy potential was about 0.85 GtCE in China in 2015. After analyzing the calculated allocation flow of bioenergy, it can be drawn that biomass power generation accounts for the highest proportion of bioenergy applications. A three-dimensional policy analysis framework is put forward to analyze the selected representative 72 pieces of biomass policies. It is concluded that there are some unbalanced policy problems, such as lacking demand policies in the biomass power generation industry and few applications of voluntary policies.

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
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    Authors: Rui Feng; Rongrong Zhang;

    In the past decades, China has adopted a wide variety of policies to stimulate bioenergy development, playing a more significant role in China’s energy structure. However, bioenergy development in China is still at an early stage and lags far behind other foreign countries. This study is aimed to explore the reasons behind this sluggish development from a policy perspective. Bioenergy development potential and provincial geographic distribution were investigated in China, which shows that the total technical bioenergy potential was about 0.85 GtCE in China in 2015. After analyzing the calculated allocation flow of bioenergy, it can be drawn that biomass power generation accounts for the highest proportion of bioenergy applications. A three-dimensional policy analysis framework is put forward to analyze the selected representative 72 pieces of biomass policies. It is concluded that there are some unbalanced policy problems, such as lacking demand policies in the biomass power generation industry and few applications of voluntary policies.

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
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    Authors: Jingxian Yang; Yifan Cheng; Jingtao Huang;

    With the rapid development of wind power, the installed capacity of wind power is also growing continuously. The intermittency and uncertainty of wind power may pose danger on the safety of the power system, thus Research of short-term load forecasting has important practical application value in the field of power network dispatching. The keys of wind power forecasting are the forecasting model selection and model optimization. In this paper, the least squares support vector machine (LSSVM) is chosen as the wind speed and the wind power prediction model and quantum-behaved particle swarm optimization (QPSO) algorithm is used to optimize the most important parameters which influence the least squares support vector machine regression model. In the proposed QPSO-LSSVM, the kernel parameter

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    Chemical Engineering Transactions
    Article . 2017
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    Authors: Jingxian Yang; Yifan Cheng; Jingtao Huang;

    With the rapid development of wind power, the installed capacity of wind power is also growing continuously. The intermittency and uncertainty of wind power may pose danger on the safety of the power system, thus Research of short-term load forecasting has important practical application value in the field of power network dispatching. The keys of wind power forecasting are the forecasting model selection and model optimization. In this paper, the least squares support vector machine (LSSVM) is chosen as the wind speed and the wind power prediction model and quantum-behaved particle swarm optimization (QPSO) algorithm is used to optimize the most important parameters which influence the least squares support vector machine regression model. In the proposed QPSO-LSSVM, the kernel parameter

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
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    Chemical Engineering Transactions
    Article . 2017
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      Chemical Engineering Transactions
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    Authors: Fredy E. Jaramillo; Pedro N. Alvarado;

    Torrefaction is a thermal pretreatment of biomass whose aim is to eliminate technical barriers of the biomass as an energy source. In this process, the raw biomass is heated in an inert atmosphere at temperatures of 200–300 °C and a low heating rate. Its purpose is converting the biomass into a carbonaceous material with improved physicochemical properties. The aim of this study was to assess the effect of torrefaction conditions on the thermal properties of a Colombian woody biomass.The results show that temperature and residence time torrefaction conditions presented a statistically significant effect on the thermal degradation of the biomass cellulose component and weight loss. In both responses, the temperature effect was higher than residence time. Besides, the residence time effect on the chemical transformation of the biomass increased when the torrefaction was more severe. TGA oxygen reactivity was measured and it was found considerable changes as the conversion of the biomass increase: high reactivity at the beginning of the oxidation reaction and diminution during the final stage of char oxidation.

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    Chemical Engineering Transactions
    Article . 2020
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    Authors: Fredy E. Jaramillo; Pedro N. Alvarado;

    Torrefaction is a thermal pretreatment of biomass whose aim is to eliminate technical barriers of the biomass as an energy source. In this process, the raw biomass is heated in an inert atmosphere at temperatures of 200–300 °C and a low heating rate. Its purpose is converting the biomass into a carbonaceous material with improved physicochemical properties. The aim of this study was to assess the effect of torrefaction conditions on the thermal properties of a Colombian woody biomass.The results show that temperature and residence time torrefaction conditions presented a statistically significant effect on the thermal degradation of the biomass cellulose component and weight loss. In both responses, the temperature effect was higher than residence time. Besides, the residence time effect on the chemical transformation of the biomass increased when the torrefaction was more severe. TGA oxygen reactivity was measured and it was found considerable changes as the conversion of the biomass increase: high reactivity at the beginning of the oxidation reaction and diminution during the final stage of char oxidation.

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
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    Chemical Engineering Transactions
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    Authors: Santanu Bandyopadhyay; Prashant Sharan;

    In multiple effect evaporators (MEE), evaporation takes place in stages; vapour coming from a stage loses its latent heat of vaporisation and acts as a heat source for the next stage. This process goes on till the last stage of evaporator where the desired concentration is achieved. MEE can be represented as a set process streams at different pressure/ temperature levels and its grand composite curve (GCC) can be generated. These process streams can be integrated with the background process to minimise the total energy consumption of the entire plant, rather than minimising the energy consumption of MEE and background process individually. An analytical methodology is developed to integrate (MEE) with the background process, such that the energy consumption for the entire pant can be minimised. A mathematical theorem is proposed to determine variation in overall energy requirement during integration of MEE with the background process. Proposed methodology is illustrated with the help of an example and up to 15.5 % of energy can be saved if the systems are integrated properly.

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    Chemical Engineering Transactions
    Article . 2015
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    Authors: Santanu Bandyopadhyay; Prashant Sharan;

    In multiple effect evaporators (MEE), evaporation takes place in stages; vapour coming from a stage loses its latent heat of vaporisation and acts as a heat source for the next stage. This process goes on till the last stage of evaporator where the desired concentration is achieved. MEE can be represented as a set process streams at different pressure/ temperature levels and its grand composite curve (GCC) can be generated. These process streams can be integrated with the background process to minimise the total energy consumption of the entire plant, rather than minimising the energy consumption of MEE and background process individually. An analytical methodology is developed to integrate (MEE) with the background process, such that the energy consumption for the entire pant can be minimised. A mathematical theorem is proposed to determine variation in overall energy requirement during integration of MEE with the background process. Proposed methodology is illustrated with the help of an example and up to 15.5 % of energy can be saved if the systems are integrated properly.

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
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      Chemical Engineering Transactions
      Article . 2015
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    Authors: Heliis Pikkor; Birgit Maaten; Zachariah Steven Baird; Oliver Järvik; +2 Authors

    Oil shale is currently used for electricity and oil production. The production of the latter produces large quantities of residue, i.e. semi-coke, from which it could be possible to create valuable porous materials with high surface areas. These adsorbents could be used in a wide range of environmental and industrial applications. To produce adsorbents, it is first important to characterise the source material and to find out to what extent the surface area differs depending on the particle size. Considering the above, seventeen oil shale fractions, with particle sizes ranging from 36 µm to 8 mm, were characterised in terms of total organic carbon (TOC) content, specific surface area (SSA) and porosity. Special attention was paid to the analysis of SSA using Brunauer-Emmett-Teller (BET) theory. The SSA of the studied oil shale was found to vary from 4 to 13 m2/g depending on the particle size. The analyses performed supported the known trend that the finer fractions have slightly higher contents of organic matter (i.e. kerogen) as well as higher surface areas. In addition, preliminary pyrolysis tests with the oil shale fractions were also carried out to see the effect of thermal treatment on surface area. After treatment, BET surface areas were in the range of 19–38 m2/g. As the final goal is to obtain activated carbon with a large SSA, it is important to know if and how much the results are affected by the source material. The present study provides fundamental knowledge about the source material that will enable applied research in the future.

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    Chemical Engineering Transactions
    Article . 2020
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      Chemical Engineering Transactions
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    Authors: Heliis Pikkor; Birgit Maaten; Zachariah Steven Baird; Oliver Järvik; +2 Authors

    Oil shale is currently used for electricity and oil production. The production of the latter produces large quantities of residue, i.e. semi-coke, from which it could be possible to create valuable porous materials with high surface areas. These adsorbents could be used in a wide range of environmental and industrial applications. To produce adsorbents, it is first important to characterise the source material and to find out to what extent the surface area differs depending on the particle size. Considering the above, seventeen oil shale fractions, with particle sizes ranging from 36 µm to 8 mm, were characterised in terms of total organic carbon (TOC) content, specific surface area (SSA) and porosity. Special attention was paid to the analysis of SSA using Brunauer-Emmett-Teller (BET) theory. The SSA of the studied oil shale was found to vary from 4 to 13 m2/g depending on the particle size. The analyses performed supported the known trend that the finer fractions have slightly higher contents of organic matter (i.e. kerogen) as well as higher surface areas. In addition, preliminary pyrolysis tests with the oil shale fractions were also carried out to see the effect of thermal treatment on surface area. After treatment, BET surface areas were in the range of 19–38 m2/g. As the final goal is to obtain activated carbon with a large SSA, it is important to know if and how much the results are affected by the source material. The present study provides fundamental knowledge about the source material that will enable applied research in the future.

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    Chemical Engineering Transactions
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    Authors: Raimonds Valdmanis; Inesa Barmina; Maija Zake;

    The experimental study and analysis of the effects of wheat straw pellets co-firing with propane flame flow and co-combustion with wood pellets on the processes of thermo-chemical conversion and heat energy production are carried out with the aim to improve the combustion conditions and applicability of wheat straw as an alternative heat energy source. The processes of wheat straw thermal decomposition and combustion of volatiles were studied experimentally using a small-scale pilot device with a heat output up to 2 kW and a test device with a heat output up to 20 kW. To improve combustion conditions, the swirl enhanced mixing of the flame components is used. The analysis of the effect of wheat straw co-firing has shown that additional heat energy supply into the biomass layer provides enhanced biomass thermal decomposition completing the combustion of volatiles and increasing thus the produced heat energy at thermo-chemical conversion of wheat straw pellets. The combustion characteristics for wheat straw pellets can be also improved by providing co- combustion of wheat straw with wood pellets. A very important result is that combustion efficiency, composition of emissions and heat output at wheat straw thermo-chemical conversion can be improved by providing co-firing and co-combustion of wheat straw with wood.

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    Chemical Engineering Transactions
    Article . 2016
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      Chemical Engineering Transactions
      Article . 2016
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    Authors: Raimonds Valdmanis; Inesa Barmina; Maija Zake;

    The experimental study and analysis of the effects of wheat straw pellets co-firing with propane flame flow and co-combustion with wood pellets on the processes of thermo-chemical conversion and heat energy production are carried out with the aim to improve the combustion conditions and applicability of wheat straw as an alternative heat energy source. The processes of wheat straw thermal decomposition and combustion of volatiles were studied experimentally using a small-scale pilot device with a heat output up to 2 kW and a test device with a heat output up to 20 kW. To improve combustion conditions, the swirl enhanced mixing of the flame components is used. The analysis of the effect of wheat straw co-firing has shown that additional heat energy supply into the biomass layer provides enhanced biomass thermal decomposition completing the combustion of volatiles and increasing thus the produced heat energy at thermo-chemical conversion of wheat straw pellets. The combustion characteristics for wheat straw pellets can be also improved by providing co- combustion of wheat straw with wood pellets. A very important result is that combustion efficiency, composition of emissions and heat output at wheat straw thermo-chemical conversion can be improved by providing co-firing and co-combustion of wheat straw with wood.

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    Chemical Engineering Transactions
    Article . 2016
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      Chemical Engineering Transactions
      Article . 2016
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    Authors: Dimitris Gkouletsos; Panos Seferlis; Athanasios I. Papadopoulos; Ibrahim Hassan;

    A systematic sensitivity analysis approach is proposed to assess the robustness of thermodynamic model predictions employed in ABR processes. A sensitivity matrix is developed which incorporates the derivatives of multiple ABR performance indicators (e.g. coefficient of performance, generated cooling, mass flowrate of working fluid etc.) with respect to multiple thermodynamic property parameters propagated through different thermodynamic prediction models. The dominant eigenvector direction of the sensitivity matrix is identified and used to explore the ABR process behaviour as indicated by the change of ABR performance indicators under simultaneous, multiple and finite thermodynamic parameter variations. This enables the robust mapping of ABR performance toward the direction of maximum variability in the multiparametric space and hence the identification of a thermodynamic model which supports robust predictions regardless of variability. The approach is illustrated in a single effect ABR process system using the NH3/H2O mixture. Among various thermodynamic models we find that the Schwartzentruber-Renon with eNRTL are the most robust combination to parameter variability.

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    Chemical Engineering Transactions
    Article . 2019
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    Authors: Dimitris Gkouletsos; Panos Seferlis; Athanasios I. Papadopoulos; Ibrahim Hassan;

    A systematic sensitivity analysis approach is proposed to assess the robustness of thermodynamic model predictions employed in ABR processes. A sensitivity matrix is developed which incorporates the derivatives of multiple ABR performance indicators (e.g. coefficient of performance, generated cooling, mass flowrate of working fluid etc.) with respect to multiple thermodynamic property parameters propagated through different thermodynamic prediction models. The dominant eigenvector direction of the sensitivity matrix is identified and used to explore the ABR process behaviour as indicated by the change of ABR performance indicators under simultaneous, multiple and finite thermodynamic parameter variations. This enables the robust mapping of ABR performance toward the direction of maximum variability in the multiparametric space and hence the identification of a thermodynamic model which supports robust predictions regardless of variability. The approach is illustrated in a single effect ABR process system using the NH3/H2O mixture. Among various thermodynamic models we find that the Schwartzentruber-Renon with eNRTL are the most robust combination to parameter variability.

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  • image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Authors: Petar Sabev Varbanov; Stanislav Boldyryev;

    This paper deals with analysis of energy consumption of Ukrainian bromine plant. Process integration allows reducing the energy consumption on 1.5 MW by heat recovery. It is achieved by improvement of recuperative heat exchangers network. Additionally heat recovery may be increased by multistage evaporation of sodium bromide and ferrous chloride. Increase the heat recovery leads utility reduction. This is not only heating and cooling duty but also power pumping and pipe heat losses. The investment for retrofit project is about 757 100 € and payback period about 2 years.

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
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    Chemical Engineering Transactions
    Article . 2014
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    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    image/svg+xml Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao Closed Access logo, derived from PLoS Open Access logo. This version with transparent background. http://commons.wikimedia.org/wiki/File:Closed_Access_logo_transparent.svg Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao
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      Chemical Engineering Transactions
      Article . 2014
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      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
      image/svg+xml Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao Closed Access logo, derived from PLoS Open Access logo. This version with transparent background. http://commons.wikimedia.org/wiki/File:Closed_Access_logo_transparent.svg Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao
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    Authors: Petar Sabev Varbanov; Stanislav Boldyryev;

    This paper deals with analysis of energy consumption of Ukrainian bromine plant. Process integration allows reducing the energy consumption on 1.5 MW by heat recovery. It is achieved by improvement of recuperative heat exchangers network. Additionally heat recovery may be increased by multistage evaporation of sodium bromide and ferrous chloride. Increase the heat recovery leads utility reduction. This is not only heating and cooling duty but also power pumping and pipe heat losses. The investment for retrofit project is about 757 100 € and payback period about 2 years.

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
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    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    Chemical Engineering Transactions
    Article . 2014
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    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
    image/svg+xml Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao Closed Access logo, derived from PLoS Open Access logo. This version with transparent background. http://commons.wikimedia.org/wiki/File:Closed_Access_logo_transparent.svg Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao
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      Chemical Engineering Transactions
      Article . 2014
      Data sources: DOAJ
      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
      image/svg+xml Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao Closed Access logo, derived from PLoS Open Access logo. This version with transparent background. http://commons.wikimedia.org/wiki/File:Closed_Access_logo_transparent.svg Jakob Voss, based on art designer at PLoS, modified by Wikipedia users Nina and Beao
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    Authors: Suoton Philip Peletiri; Iqbal M. Mujtaba; Nejat Rahmanian;

    With about 195 countries signing the Paris (climate) Agreement and world leaders uniting for the planet after the United States’ notification to pull out of the agreement, many carbon capture and storage (CCS) projects are expected to be executed worldwide. Captured CO2 is not pure and may contain several impurities, which affect the flow dynamics of the CO2 fluid in pipelines. To design efficient CO2 pipeline transportation systems, it is imperative to understand the effect of these impurities on the flow behaviour. Aspen HYSYS (V10) and HydraFlash were used to study the behaviour of 90 mol % CO2 and 10 mol % single impurity (N2, CH4, H2, H2S, SO2, Ar, CO, NH3, O2 and H2O). The Peng-Robinson equation of state (EoS), which has the lowest average absolute deviation (AAD) among cubic EoS for predicting CO2 fluid properties, was used in Aspen HYSYS. Three different 50 km pipelines were simulated; one horizontal pipeline and two pipelines with +300 and -300 m in elevation between inlet and outlet respectively. The mass flow rate is 266,400 kg/h and the internal and external diameters of the pipelines are 0.289 m and 0.324 m respectively. All impurities changed the parameters of the flowing fluid. H2 impurity caused the most pressure loss for horizontal pipelines but may cause the least pressure loss for pipelines at high inclination angles. H2 and H2S formed the widest and narrowest two-phase regions, respectively. The results also show that H2 impurity resulted in the most heat loss while H2O and SO2 impurities had the lowest heat losses. Pipeline elevation change also affects the effect of each impurity on pressure changes. The difference in pressure drop between the impurity with the highest effect, H2, and that with the least effect, SO2, is 0.44 MPa for inclined pipelines, 0.77 MPa for horizontal pipelines and 1.44 MPa for declined pipelines. H2S had the mildest effect followed by NH3, H2O, SO2, CO, Ar, CH4, O2, N2 and H2.

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
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    Chemical Engineering Transactions
    Article . 2018
    Data sources: DOAJ
    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
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      Chemical Engineering Transactions
      Article . 2018
      Data sources: DOAJ
      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
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    Authors: Suoton Philip Peletiri; Iqbal M. Mujtaba; Nejat Rahmanian;

    With about 195 countries signing the Paris (climate) Agreement and world leaders uniting for the planet after the United States’ notification to pull out of the agreement, many carbon capture and storage (CCS) projects are expected to be executed worldwide. Captured CO2 is not pure and may contain several impurities, which affect the flow dynamics of the CO2 fluid in pipelines. To design efficient CO2 pipeline transportation systems, it is imperative to understand the effect of these impurities on the flow behaviour. Aspen HYSYS (V10) and HydraFlash were used to study the behaviour of 90 mol % CO2 and 10 mol % single impurity (N2, CH4, H2, H2S, SO2, Ar, CO, NH3, O2 and H2O). The Peng-Robinson equation of state (EoS), which has the lowest average absolute deviation (AAD) among cubic EoS for predicting CO2 fluid properties, was used in Aspen HYSYS. Three different 50 km pipelines were simulated; one horizontal pipeline and two pipelines with +300 and -300 m in elevation between inlet and outlet respectively. The mass flow rate is 266,400 kg/h and the internal and external diameters of the pipelines are 0.289 m and 0.324 m respectively. All impurities changed the parameters of the flowing fluid. H2 impurity caused the most pressure loss for horizontal pipelines but may cause the least pressure loss for pipelines at high inclination angles. H2 and H2S formed the widest and narrowest two-phase regions, respectively. The results also show that H2 impurity resulted in the most heat loss while H2O and SO2 impurities had the lowest heat losses. Pipeline elevation change also affects the effect of each impurity on pressure changes. The difference in pressure drop between the impurity with the highest effect, H2, and that with the least effect, SO2, is 0.44 MPa for inclined pipelines, 0.77 MPa for horizontal pipelines and 1.44 MPa for declined pipelines. H2S had the mildest effect followed by NH3, H2O, SO2, CO, Ar, CH4, O2, N2 and H2.

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
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    Chemical Engineering Transactions
    Article . 2018
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    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
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      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
      Chemical Engineering Transactions
      Article . 2018
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      image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
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    Authors: G. Cantarelli Lopes; L. Machado Da Rosa; M. Mori; J.R. Nunhez; +1 Authors

    Abstract preview not available - see full-text PDF article.

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    Chemical Engineering Transactions
    Article . 2011
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      Chemical Engineering Transactions
      Article . 2011
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    Authors: G. Cantarelli Lopes; L. Machado Da Rosa; M. Mori; J.R. Nunhez; +1 Authors

    Abstract preview not available - see full-text PDF article.

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
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    Chemical Engineering Transactions
    Article . 2011
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      Chemical Engineering Transactions
      Article . 2011
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    Authors: Rui Feng; Rongrong Zhang;

    In the past decades, China has adopted a wide variety of policies to stimulate bioenergy development, playing a more significant role in China’s energy structure. However, bioenergy development in China is still at an early stage and lags far behind other foreign countries. This study is aimed to explore the reasons behind this sluggish development from a policy perspective. Bioenergy development potential and provincial geographic distribution were investigated in China, which shows that the total technical bioenergy potential was about 0.85 GtCE in China in 2015. After analyzing the calculated allocation flow of bioenergy, it can be drawn that biomass power generation accounts for the highest proportion of bioenergy applications. A three-dimensional policy analysis framework is put forward to analyze the selected representative 72 pieces of biomass policies. It is concluded that there are some unbalanced policy problems, such as lacking demand policies in the biomass power generation industry and few applications of voluntary policies.

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
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    Chemical Engineering Transactions
    Article . 2021
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    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/
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      Chemical Engineering Transactions
      Article . 2021
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    Authors: Rui Feng; Rongrong Zhang;

    In the past decades, China has adopted a wide variety of policies to stimulate bioenergy development, playing a more significant role in China’s energy structure. However, bioenergy development in China is still at an early stage and lags far behind other foreign countries. This study is aimed to explore the reasons behind this sluggish development from a policy perspective. Bioenergy development potential and provincial geographic distribution were investigated in China, which shows that the total technical bioenergy potential was about 0.85 GtCE in China in 2015. After analyzing the calculated allocation flow of bioenergy, it can be drawn that biomass power generation accounts for the highest proportion of bioenergy applications. A three-dimensional policy analysis framework is put forward to analyze the selected representative 72 pieces of biomass policies. It is concluded that there are some unbalanced policy problems, such as lacking demand policies in the biomass power generation industry and few applications of voluntary policies.

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    Chemical Engineering Transactions
    Article . 2021
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      Chemical Engineering Transactions
      Article . 2021
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    Authors: Jingxian Yang; Yifan Cheng; Jingtao Huang;

    With the rapid development of wind power, the installed capacity of wind power is also growing continuously. The intermittency and uncertainty of wind power may pose danger on the safety of the power system, thus Research of short-term load forecasting has important practical application value in the field of power network dispatching. The keys of wind power forecasting are the forecasting model selection and model optimization. In this paper, the least squares support vector machine (LSSVM) is chosen as the wind speed and the wind power prediction model and quantum-behaved particle swarm optimization (QPSO) algorithm is used to optimize the most important parameters which influence the least squares support vector machine regression model. In the proposed QPSO-LSSVM, the kernel parameter

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    Chemical Engineering Transactions
    Article . 2017
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      Chemical Engineering Transactions
      Article . 2017
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    Authors: Jingxian Yang; Yifan Cheng; Jingtao Huang;

    With the rapid development of wind power, the installed capacity of wind power is also growing continuously. The intermittency and uncertainty of wind power may pose danger on the safety of the power system, thus Research of short-term load forecasting has important practical application value in the field of power network dispatching. The keys of wind power forecasting are the forecasting model selection and model optimization. In this paper, the least squares support vector machine (LSSVM) is chosen as the wind speed and the wind power prediction model and quantum-behaved particle swarm optimization (QPSO) algorithm is used to optimize the most important parameters which influence the least squares support vector machine regression model. In the proposed QPSO-LSSVM, the kernel parameter

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
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    Chemical Engineering Transactions
    Article . 2017
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      Chemical Engineering Transactions
      Article . 2017
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    Authors: Fredy E. Jaramillo; Pedro N. Alvarado;

    Torrefaction is a thermal pretreatment of biomass whose aim is to eliminate technical barriers of the biomass as an energy source. In this process, the raw biomass is heated in an inert atmosphere at temperatures of 200–300 °C and a low heating rate. Its purpose is converting the biomass into a carbonaceous material with improved physicochemical properties. The aim of this study was to assess the effect of torrefaction conditions on the thermal properties of a Colombian woody biomass.The results show that temperature and residence time torrefaction conditions presented a statistically significant effect on the thermal degradation of the biomass cellulose component and weight loss. In both responses, the temperature effect was higher than residence time. Besides, the residence time effect on the chemical transformation of the biomass increased when the torrefaction was more severe. TGA oxygen reactivity was measured and it was found considerable changes as the conversion of the biomass increase: high reactivity at the beginning of the oxidation reaction and diminution during the final stage of char oxidation.

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    Chemical Engineering Transactions
    Article . 2020
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      Chemical Engineering Transactions
      Article . 2020
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    Authors: Fredy E. Jaramillo; Pedro N. Alvarado;

    Torrefaction is a thermal pretreatment of biomass whose aim is to eliminate technical barriers of the biomass as an energy source. In this process, the raw biomass is heated in an inert atmosphere at temperatures of 200–300 °C and a low heating rate. Its purpose is converting the biomass into a carbonaceous material with improved physicochemical properties. The aim of this study was to assess the effect of torrefaction conditions on the thermal properties of a Colombian woody biomass.The results show that temperature and residence time torrefaction conditions presented a statistically significant effect on the thermal degradation of the biomass cellulose component and weight loss. In both responses, the temperature effect was higher than residence time. Besides, the residence time effect on the chemical transformation of the biomass increased when the torrefaction was more severe. TGA oxygen reactivity was measured and it was found considerable changes as the conversion of the biomass increase: high reactivity at the beginning of the oxidation reaction and diminution during the final stage of char oxidation.

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    Chemical Engineering Transactions
    Article . 2020
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      Chemical Engineering Transactions
      Article . 2020
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    Authors: Santanu Bandyopadhyay; Prashant Sharan;

    In multiple effect evaporators (MEE), evaporation takes place in stages; vapour coming from a stage loses its latent heat of vaporisation and acts as a heat source for the next stage. This process goes on till the last stage of evaporator where the desired concentration is achieved. MEE can be represented as a set process streams at different pressure/ temperature levels and its grand composite curve (GCC) can be generated. These process streams can be integrated with the background process to minimise the total energy consumption of the entire plant, rather than minimising the energy consumption of MEE and background process individually. An analytical methodology is developed to integrate (MEE) with the background process, such that the energy consumption for the entire pant can be minimised. A mathematical theorem is proposed to determine variation in overall energy requirement during integration of MEE with the background process. Proposed methodology is illustrated with the help of an example and up to 15.5 % of energy can be saved if the systems are integrated properly.

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    Chemical Engineering Transactions
    Article . 2015
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      Chemical Engineering Transactions
      Article . 2015
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    Authors: Santanu Bandyopadhyay; Prashant Sharan;

    In multiple effect evaporators (MEE), evaporation takes place in stages; vapour coming from a stage loses its latent heat of vaporisation and acts as a heat source for the next stage. This process goes on till the last stage of evaporator where the desired concentration is achieved. MEE can be represented as a set process streams at different pressure/ temperature levels and its grand composite curve (GCC) can be generated. These process streams can be integrated with the background process to minimise the total energy consumption of the entire plant, rather than minimising the energy consumption of MEE and background process individually. An analytical methodology is developed to integrate (MEE) with the background process, such that the energy consumption for the entire pant can be minimised. A mathematical theorem is proposed to determine variation in overall energy requirement during integration of MEE with the background process. Proposed methodology is illustrated with the help of an example and up to 15.5 % of energy can be saved if the systems are integrated properly.

    image/svg+xml art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos Open Access logo, converted into svg, designed by PLoS. This version with transparent background. http://commons.wikimedia.org/wiki/File:Open_Access_logo_PLoS_white.svg art designer at PLoS, modified by Wikipedia users Nina, Beao, JakobVoss, and AnonMoos http://www.plos.org/ Chemical Engineering...arrow_drop_down
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    Chemical Engineering Transactions
    Article . 2015
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      Chemical Engineering Transactions
      Article . 2015
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    Authors: Heliis Pikkor; Birgit Maaten; Zachariah Steven Baird; Oliver Järvik; +2 Authors

    Oil shale is currently used for electricity and oil production. The production of the latter produces large quantities of residue, i.e. semi-coke, from which it could be possible to create valuable porous materials with high surface areas. These adsorbents could be used in a wide range of environmental and industrial applications. To produce adsorbents, it is first important to characterise the source material and to find out to what extent the surface area differs depending on the particle size. Considering the above, seventeen oil shale fractions, with particle sizes ranging from 36 µm to 8 mm, were characterised in terms of total organic carbon (TOC) content, specific surface area (SSA) and porosity. Special attention was paid to the analysis of SSA using Brunauer-Emmett-Teller (BET) theory. The SSA of the studied oil shale was found to vary from 4 to 13 m2/g depending on the particle size. The analyses performed supported the known trend that the finer fractions have slightly higher contents of organic matter (i.e. kerogen) as well as higher surface areas. In addition, preliminary pyrolysis tests with the oil shale fractions were also carried out to see the effect of thermal treatment on surface area. After treatment, BET surface areas were in the range of 19–38 m2/g. As the final goal is to obtain activated carbon with a large SSA, it is important to know if and how much the results are affected by the source material. The present study provides fundamental knowledge about the source material that will enable applied research in the future.

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    Chemical Engineering Transactions
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      Chemical Engineering Transactions
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    Authors: Heliis Pikkor; Birgit Maaten; Zachariah Steven Baird; Oliver Järvik; +2 Authors

    Oil shale is currently used for electricity and oil production. The production of the latter produces large quantities of residue, i.e. semi-coke, from which it could be possible to create valuable porous materials with high surface areas. These adsorbents could be used in a wide range of environmental and industrial applications. To produce adsorbents, it is first important to characterise the source material and to find out to what extent the surface area differs depending on the particle size. Considering the above, seventeen oil shale fractions, with particle sizes ranging from 36 µm to 8 mm, were characterised in terms of total organic carbon (TOC) content, specific surface area (SSA) and porosity. Special attention was paid to the analysis of SSA using Brunauer-Emmett-Teller (BET) theory. The SSA of the studied oil shale was found to vary from 4 to 13 m2/g depending on the particle size. The analyses performed supported the known trend that the finer fractions have slightly higher contents of organic matter (i.e. kerogen) as well as higher surface areas. In addition, preliminary pyrolysis tests with the oil shale fractions were also carried out to see the effect of thermal treatment on surface area. After treatment, BET surface areas were in the range of 19–38 m2/g. As the final goal is to obtain activated carbon with a large SSA, it is important to know if and how much the results are affected by the source material. The present study provides fundamental knowledge about the source material that will enable applied research in the future.

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    Chemical Engineering Transactions
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      Chemical Engineering Transactions
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    Authors: Raimonds Valdmanis; Inesa Barmina; Maija Zake;

    The experimental study and analysis of the effects of wheat straw pellets co-firing with propane flame flow and co-combustion with wood pellets on the processes of thermo-chemical conversion and heat energy production are carried out with the aim to improve the combustion conditions and applicability of wheat straw as an alternative heat energy source. The processes of wheat straw thermal decomposition and combustion of volatiles were studied experimentally using a small-scale pilot device with a heat output up to 2 kW and a test device with a heat output up to 20 kW. To improve combustion conditions, the swirl enhanced mixing of the flame components is used. The analysis of the effect of wheat straw co-firing has shown that additional heat energy supply into the biomass layer provides enhanced biomass thermal decomposition completing the combustion of volatiles and increasing thus the produced heat energy at thermo-chemical conversion of wheat straw pellets. The combustion characteristics for wheat straw pellets can be also improved by providing co- combustion of wheat straw with wood pellets. A very important result is that combustion efficiency, composition of emissions and heat output at wheat straw thermo-chemical conversion can be improved by providing co-firing and co-combustion of wheat straw with wood.

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    Chemical Engineering Transactions
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      Chemical Engineering Transactions
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    Authors: Raimonds Valdmanis; Inesa Barmina; Maija Zake;

    The experimental study and analysis of the effects of wheat straw pellets co-firing with propane flame flow and co-combustion with wood pellets on the processes of thermo-chemical conversion and heat energy production are carried out with the aim to improve the combustion conditions and applicability of wheat straw as an alternative heat energy source. The processes of wheat straw thermal decomposition and combustion of volatiles were studied experimentally using a small-scale pilot device with a heat output up to 2 kW and a test device with a heat output up to 20 kW. To improve combustion conditions, the swirl enhanced mixing of the flame components is used. The analysis of the effect of wheat straw co-firing has shown that additional heat energy supply into the biomass layer provides enhanced biomass thermal decomposition completing the combustion of volatiles and increasing thus the produced heat energy at thermo-chemical conversion of wheat straw pellets. The combustion characteristics for wheat straw pellets can be also improved by providing co- combustion of wheat straw with wood pellets. A very important result is that combustion efficiency, composition of emissions and heat output at wheat straw thermo-chemical conversion can be improved by providing co-firing and co-combustion of wheat straw with wood.

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    Chemical Engineering Transactions
    Article . 2016
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      Chemical Engineering Transactions
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    Authors: Dimitris Gkouletsos; Panos Seferlis; Athanasios I. Papadopoulos; Ibrahim Hassan;

    A systematic sensitivity analysis approach is proposed to assess the robustness of thermodynamic model predictions employed in ABR processes. A sensitivity matrix is developed which incorporates the derivatives of multiple ABR performance indicators (e.g. coefficient of performance, generated cooling, mass flowrate of working fluid etc.) with respect to multiple thermodynamic property parameters propagated through different thermodynamic prediction models. The dominant eigenvector direction of the sensitivity matrix is identified and used to explore the ABR process behaviour as indicated by the change of ABR performance indicators under simultaneous, multiple and finite thermodynamic parameter variations. This enables the robust mapping of ABR performance toward the direction of maximum variability in the multiparametric space and hence the identification of a thermodynamic model which supports robust predictions regardless of variability. The approach is illustrated in a single effect ABR process system using the NH3/H2O mixture. Among various thermodynamic models we find that the Schwartzentruber-Renon with eNRTL are the most robust combination to parameter variability.

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    Chemical Engineering Transactions
    Article . 2019
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    Authors: Dimitris Gkouletsos; Panos Seferlis; Athanasios I. Papadopoulos; Ibrahim Hassan;

    A systematic sensitivity analysis approach is proposed to assess the robustness of thermodynamic model predictions employed in ABR processes. A sensitivity matrix is developed which incorporates the derivatives of multiple ABR performance indicators (e.g. coefficient of performance, generated cooling, mass flowrate of working fluid etc.) with respect to multiple thermodynamic property parameters propagated through different thermodynamic prediction models. The dominant eigenvector direction of the sensitivity matrix is identified and used to explore the ABR process behaviour as indicated by the change of ABR performance indicators under simultaneous, multiple and finite thermodynamic parameter variations. This enables the robust mapping of ABR performance toward the direction of maximum variability in the multiparametric space and hence the identification of a thermodynamic model which supports robust predictions regardless of variability. The approach is illustrated in a single effect ABR process system using the NH3/H2O mixture. Among various thermodynamic models we find that the Schwartzentruber-Renon with eNRTL are the most robust combination to parameter variability.

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    Chemical Engineering Transactions
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