Zobrazeno 1 - 10
of 19
pro vyhledávání: '"Gheorghe Bumbac"'
Autor:
Gheorghe Bumbac, Ionut Banu
Publikováno v:
Renewable Energy. 183:662-675
The increasing biodiesel production generates important amounts of glycerol, by-product that require the development of new and sustainable processes in order to be converted into value added chemicals. In this paper special attention was given to po
Publikováno v:
Industrial & Engineering Chemistry Research. 60:13071-13083
Publikováno v:
Renewable Energy. 148:548-557
An important category of glycerol derivatives, having multiple practical applications, are its esters with acetic acid (acetates or acetins). The most common preparation method of glycerol acetates is the direct esterification of glycerol with acetic
Autor:
Augustin Crucean, Ana-Maria Galan, Grigore Bozga, Mihaela Bombos, Gheorghe Bumbac, Ionut Banu, Alin Vintila, Olimpiu Blajan, Sanda Velea
Publikováno v:
Scopus-Elsevier
The increased quantities of glycerol available on the market initiated research efforts oriented to new valorization technologies, particularly by its conversion into medium tonnage chemicals, replacing petroleum derivatives. In this work it was inve
Publikováno v:
Renewable Energy. 131:137-143
The present paper evaluates the feasibility of a process flowsheet for butanol bioproduction, as pure compound or as a blend with the biodiesel used as the liquid-liquid extraction (LLEx) solvent. In order to evidence this aspect, a modeling and simu
Publikováno v:
Applied Thermal Engineering. 23:1857-1869
The paper presents an industrial case study. Crude distillation unit (CDU) and delayed coking unit (DCU) are important plants in oil refineries, presenting huge energy consumption, especially due to high flowrates of process material streams. Any acc
Autor:
Valentin Plesu, Jordi Bonet-Ruiz, Bertram Muchan, Petrica Iancu, Gheorghe Bumbac, Olivia A. Perederic, Alexandra-Elena Bonet-Ruiz
A new sustainable process to produce tert-amyl-methyl-ether (TAME) using as feedstock enriched C 5 fraction (LCN – light cracking naphtha) from catalytic cracking (FCC) is developed. Existing technologies are based on methanol (MeOH) separation by
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::9d68890dc3b6339b31496f055b42ba72
https://doi.org/10.1016/b978-0-444-63455-9.50083-0
https://doi.org/10.1016/b978-0-444-63455-9.50083-0
This contribution aims to present a methodology to model and simulate the reactive dividing wall column (RDWC) using commercial software. Feasibility of separation scheme was established with ASPEN DISTIL™. Simulation of flowsheet configuration was
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::af24dd8602dade12b6c6158fef7376bb
https://doi.org/10.1016/s1570-7946(07)80097-6
https://doi.org/10.1016/s1570-7946(07)80097-6
Catalytic distillation (CD), involving reaction and separation in the same unit, is possible and beneficial when both volatility of reactants is close each other, but quite different from the volatility of products, and the conversion is limited by c
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::e17a50ee87b2a1f127917c345da52103
https://doi.org/10.1016/s1570-7946(05)80231-7
https://doi.org/10.1016/s1570-7946(05)80231-7
The work presents a simulation study of a reactive distillation (RD) unit for tert-amyl-methyl-ether synthesis using HYSYSTM simulation environment. In order to simulate the RD column this was represented as an ensemble of three components correspond
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::f7f0db495b001ac2f47edb088b8b7b60
https://doi.org/10.1016/s1570-7946(03)80177-3
https://doi.org/10.1016/s1570-7946(03)80177-3