Industrial & Engineering Chemistry Research (IND ENG CHEM RES )

Publisher: American Chemical Society, American Chemical Society

Description

For industrial chemists and chemical engineers, Industrial & Engineering Chemistry Research is the reliable and current source of new fundamental research, design methods, process design and development, and product research and development. This state-of-the art journal contains original studies in the areas of: Applied Chemistry, Kinetics, Catalysis, and Reaction Engineering, Materials and Interfaces, Process, Design and Control, Separations, General Research.

  • Impact factor
    2.24
    Show impact factor history
     
    Impact factor
  • 5-year impact
    2.46
  • Cited half-life
    6.90
  • Immediacy index
    0.42
  • Eigenfactor
    0.07
  • Article influence
    0.64
  • Website
    Industrial & Engineering Chemistry Research website
  • Other titles
    Industrial & engineering chemistry research, Industrial and engineering chemistry research, I & EC research
  • ISSN
    0888-5885
  • OCLC
    13659424
  • Material type
    Periodical, Internet resource
  • Document type
    Journal / Magazine / Newspaper, Internet Resource

Publisher details

American Chemical Society

  • Pre-print
    • Author cannot archive a pre-print version
  • Restrictions
    • Must obtain written permission from Editor
    • Must not violate ACS ethical Guidelines
  • Post-print
    • Author cannot archive a post-print version
  • Restrictions
    • If mandated by funding agency or employer/ institution
    • If mandated to deposit before 12 months, must obtain waiver from Institution/Funding agency or use AuthorChoice
    • 12 months embargo
  • Conditions
    • On author's personal website, pre-print servers, institutional website, institutional repositories or subject repositories
    • Non-Commercial
    • Must be accompanied by set statement (see policy)
    • Must link to publisher version
    • Publisher's version/PDF cannot be used
    • If mandated sooner than 12 months, must obtain waiver from Editors or use AuthorChoice
    • Reviewed on 07/08/2014
  • Classification
    ​ white

Publications in this journal

  • Industrial & Engineering Chemistry Research 01/2015;
  • Industrial & Engineering Chemistry Research 01/2015;
  • [Show abstract] [Hide abstract]
    ABSTRACT: The volatility of the global oil market, coupled with increasing levels of greenhouse gas (GHG) emissions, has sparked the search for alternative methods for the production of liquid transportation fuels from domestically available carbon-based resources. The United States has three feedstocks available to gradually replace petroleum as its primary energy source, namely: coal, biomass, and natural gas. The major contributions to the production of liquid fuels from these three feedstocks have been highlighted in a recent review [1]. Hybrid energy systems utilizing coal and biomass have been the center of interest in recent years. Coal has a lower delivered cost than biomass, but conventional coal-to-liquids (CTL) refineries result in almost twice the life-cycle GHG emissions of a petroleum-based plant. Biomass, however, has the ability to reduce greenhouse gas emissions through the capture of CO2 during photosynthesis. The economic and environmental benefits that both these feedstocks offer can be exploited by investigating coal-and-biomass-to-liquid fuels (CBTL) systems. Using an optimization-based process synthesis framework, the thermochemical conversion of coal and biomass will be presented [2]. Synthesis gas (syngas) will be generated via gasification of the biomass and coal feedstocks through separate gasification units. The syngas can then be directed to either a dedicated water-gas-shift reactor or passed directly to the scrubbing system. Hydrocarbon production will proceed through either Fischer-Tropsch synthesis or methanol formation. The Fischer-Tropsch hydrocarbons can be upgraded over a ZSM-5 reactor or through a series of treatment units that will produce distillate and gasoline-range products. The methanol can be passed to the methanol-to-gasoline (MTG) process or to the methanol-to-olefins/olefins-to-gasoline-and-distillate (MTO/MOGD) processes. Simultaneous heat and power integration is included in the model to convert waste heat into electricity. The optimal process topology that can produce gasoline, diesel, and kerosene at the lowest cost is determined using rigorous deterministic global optimization and process synthesis strategies [3-13]. This study presents a baseline so that a fair comparison between different process alternatives can be made. Multiple case studies are presented to investigate the effect of plant capacity and product distribution on the overall cost of the refinery, the process topology, the total plant cost, and the break-even oil price. The results demonstrate that coal and biomass refineries can become economically competitive with petroleum-based processes while simultaneously reducing life-cycle greenhouse gas emissions. [1] Floudas, C. A.; Elia, J. A.; Baliban, R. C. Hybrid and single feedstock energy processes for liquid transportation fuels: A critical review. Computers & Chemical Engineering 2012, 41 (6), 24-51. [2] Niziolek, A. M.; Onel, O.; Elia, J. A.; Baliban, R. C.; Xiao, X.; Floudas, C. A. Coal and Biomass to Liquid Transportation Fuels: Process Synthesis and Global Optimization Strategies. Industrial & Engineering Chemistry Research 2014 DOI: 10.1021/ie500505h. [3] Baliban, R. C., Elia, J. A., Floudas, C. A. Toward novel biomass, coal, and natural gas processes for satisfying current transportation fuel demands, 1: Process alternatives, gasification modeling, process simulation, and economic analysis. Industrial & Engineering Chemistry Research 2010, 49, 7343-7370. [4] Elia, J. A., Baliban, R. C., Floudas, C. A. Toward novel biomass, coal, and natural gas processes for satisfying current transportation fuel demands, 2: Simultaneous heat and power integration. Industrial & Engineering Chemistry Research 2010, 49, 7371-7388. [5] Baliban, R. C., Elia, J. A., Floudas, C. A. Optimization framework for the simultaneous process synthesis, heat and power integration of a thermochemical hybrid biomass, coal, and natural gas facility. Comp. Chem. Eng. 2011, 35, 1647-1690. [6] Baliban, R. C., Elia, J. A., Floudas, C. A. Simultaneous process synthesis, heat, power, and water integration of thermochemical hybrid biomass, coal, and natural gas facilities. Comp. Chem. Eng. 2012, 37, 297-327. [7] Baliban, R. C., Elia, J. A., Misener, R., Floudas, C. A. Global Optimization of a MINLP Process Synthesis Model for Thermochemical Based Conversion of Hybrid Coal, Biomass, and Natural Gas to Liquid Fuels. Comp. Chem. Eng. 2012, 42, 64-86. [8] Baliban, R. C., Elia, J. A., Weekman, V., Floudas, C. A. Process Synthesis of Hybrid Coal, Biomass, and Natural Gas to Liquids via Fischer-Tropsch Synthesis, ZSM-5 Catalytic Conversion, Methanol Synthesis, Methanol-to-Gasoline, and Methanol-to-Olefins/Distillate Technologies. Comp. Chem. Eng. 2012, 47 (12), 29-56. [9] Baliban, R. C.; Elia, J. A.; Floudas, C. A. Biomass to liquid transportation fuels (BTL) systems: process synthesis and global optimization framework. Energy Environ. Sci. 2013, 6 (1), 267-287. [10] Baliban, R. C.; Elia, J. A.; Floudas, C. A. Novel Natural Gas to Liquids Processes: Process Synthesis and Global Optimization Strategies. AIChE Journal 2013, 59 (2), 505-531. [11] Baliban, R. C.; Elia, J. A.; Floudas, C. A. Biomass and Natural Gas to Liquid Transportation Fuels: Process Synthesis, Global Optimization, and Topology Analysis. Industrial & Engineering Chemistry Research 2013, 52 (9), 3381-3406. [12] Baliban, R. C.; Elia, J. A.; Floudas, C. A.; Gurau, B.; Weingarten, M. B.; Klotz, S. D. Hardwood Biomass to Gasoline, Diesel, and Jet Fuel: 1. Process Synthesis and Global Optimization of a Thermochemical Refinery. Energy & Fuels 2013, 27 (8), 4302-4324. [13] Baliban, R. C.; Elia, J. A.; Floudas, C. A.; Xiao, X.; Zhang, Z.; Li, J.; Cao, H.; Ma, J.; Qiao, Y.; Hu, X. Thermochemical Conversion of Duckweed Biomass to Gasoline, Diesel, and Jet Fuel: Process Synthesis and Global Optimization. Industrial & Engineering Chemistry Research 2013, 52 (33), 11436-11450.
    14 AIChE Annual Meeting; 11/2014
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    ABSTRACT: Decomposition of gaseous NH3 from ammonia (NH3)-containing wastewater was explored using Ni-loading Al2O3 catalysts. The thermochemical decomposition of an NH3/steam mixture (wet-NH3) with different steam contents at 873, 923, and 973 K using a fixed-bed reactor under ambient pressure. The present results indicated that the catalysts can be deactivated by the formation of NiAl2O4, which can be thermodynamically generated, and confirmed that the extent of deactivation was greatly affected by the partial pressure of the steam (PH2O). The catalytic activities at 873 K decreased with increasing PH2O, whereas the activity was constant above PH2O of 25 kPa. However, the NH3 conversion was almost independent of the NH3 flow rate and temperature, and ∼30% of the NH3 was decomposed at each temperature. This study indicated that, even in the presence of steam, this catalyst could decompose NH3 from NH4+-containing water.
    Industrial & Engineering Chemistry Research 11/2014; 53 (45):17849–17853.
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    ABSTRACT: A comprehensive investigation of wastewater treatment operation is provided through utilization of a validated dynamic model, historical data from a real plant, and bifurcation theory. Bifurcation analysis was carried out with wastewater flow rate, stormwater flow rate, airflow rate, water temperature, and influent ammonia concentration as the free parameters. A two-parameter continuation using airflow rate and water temperature simultaneously was also performed. Results indicate an overall robustness of the plant toward disturbances, which comes at the cost of excessive energy usage. Even then, transients caused by those disturbances are inevitable and can cause violations of regulatory permits on effluent ammonia and dissolved oxygen concentrations. Another important finding is the excessive air usage in aeration tanks, which can be cut by 50% on average without affecting the effluent quality.
    Industrial & Engineering Chemistry Research 10/2014; 53(45):17736-17752.
  • Industrial & Engineering Chemistry Research 09/2014; 53(42):16550-16558.
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    ABSTRACT: In this study, multiwalled carbon nanotubes were successfully modified using poly propyleneimine dendrimer. Structural characterization of the newly synthesized adsorbent confirmed the modification of nanotubes by dendrimer molecules. In order to evaluate the performance of this novel adsorbent for the removal of two direct dyes from textile wastewaters, the effect of important parameters including pH, initial dye concentration, adsorbent dosage, and inorganic salts was investigated in single and binary dye solutions. Response surface methodology was employed to find the relation between the effective parameters and dye removal efficiency. The adsorption process was optimized to reach the dye removal of 95% using response optimizer. The prepared adsorbent showed excellent adsorption behavior toward the anionic dye molecules, and the dye removal efficiencies of nanotubes were significantly improved from 17.7% to 99.9% after their modification with dendrimer. Also, the desorption tests revealed the maximum dye release of 44.01%.
    Industrial & Engineering Chemistry Research 09/2014; 53(38):14841-14853.
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    ABSTRACT: The presence of aromatics such as benzene, toluene and xylene (BTX) as contaminants in H2S gas stream entering Claus sulfur recovery units has detrimental effect on catalytic reactors, where BTX form soot particles, and clog and deactivate the catalysts. BTX oxidation, before they enter catalyst beds, can solve this problem. A theoretical investigation is presented on toluene oxidation by SO2. Density functional theory is used to study toluene radicals (benzyl, o-methylphenyl, m-methylphenyl and p-methylphenyl)–SO2 interactions. The mechanism begins with SO2 addition on the radical through one of the O atoms rather than the S atom. This exothermic reaction involves energy barriers of 4.8-6.1 kJ/mol for different toluene radicals. Thereafter, O—S bond scission takes place to release SO. The reaction rate constants are evaluated to facilitate process simulations. Among four toluene radicals, the resonantly stabilized benzyl radical exhibited lowest SO2 addition rate. A remarkable similarity between toluene oxidation by O2 and by SO2 is observed.
    Industrial & Engineering Chemistry Research 09/2014;