Zobrazeno 1 - 10
of 12
pro vyhledávání: '"Carlos Daniel Fischer"'
Publikováno v:
Industrial & Engineering Chemistry Research. 59:21155-21166
Separation vessels are traditionally designed based on rules of thumb that guide the designer to a feasible solution. Despite its widespread use, this approach presents important limitations, which...
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::d1811f4a7dd1681ac1dd3f37d855c33c
https://doi.org/10.1021/acs.iecr.0c04379
https://doi.org/10.1021/acs.iecr.0c04379
MILP APPROACH FOR THE DESIGN OF VERTICAL VAPOR-LIQUID SEPARATION VESSELS- COMPARISON WITH HEURISTICS
Publikováno v:
Latin American Applied Research - An international journal. 50:65-70
In this article we compare results from different heuristics approaches for the design of VLE separation vessels. In addition, we present an MILP model that embeds the aforementioned heuristics and considers the discrete nature of the geometric varia
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::8faa64b224aa10ebe2e9617b9c33152b
https://doi.org/10.52292/j.laar.2020.204
https://doi.org/10.52292/j.laar.2020.204
Publikováno v:
International Journal of Hydrogen Energy. 44:13509-13522
For our works, Mass Exchangers (MEs) are membrane equipment that exchange some component between two streams in a countercurrent arrangement. In previous works these were proposed to use them (with the goal of hydrogen recovery, energy saving and was
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::1f67b9b7bf7805c5b7c7f3f5c48ccb3b
https://doi.org/10.1016/j.ijhydene.2019.04.001
https://doi.org/10.1016/j.ijhydene.2019.04.001
Publikováno v:
International Journal of Hydrogen Energy. 41:2399-2410
In this work we analyze different design alternatives for the integration of a gasification process with the oxygen production process, through ITM membranes. We analyze the conventional separation design compared with a novel configuration in a coun
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::b5ce92aa33fc36cae66642fb82acac63
https://doi.org/10.1016/j.ijhydene.2015.12.124
https://doi.org/10.1016/j.ijhydene.2015.12.124
In this work, we propose a new arrangement for integrating an Autothermal Reforming of Ethanol process with oxygen production with the technology of ITM membranes. In the conventional configuration O2is first separated from the air and then injected
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::b9a06022b88599741f4ac345efa6673c
http://www.sciencedirect.com/science/article/pii/S0098135417300480
http://www.sciencedirect.com/science/article/pii/S0098135417300480
In this work a model is proposed to select among process alternatives that take soapstock as raw material, with the aim of maximizing economical performance, as well as disposing soapstock in an environmentally conscious way. This aim has been approa
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::75265726083d0f683583f558f3bc15b3
https://www.sciencedirect.com/science/article/pii/S0960308516301511
https://www.sciencedirect.com/science/article/pii/S0960308516301511
Publikováno v:
International Journal of Hydrogen Energy. 39:20094-20104
In this paper, we propose a novel hydrogen recovery structure in a cyclohexane production process, arrived at by following a mass exchange heuristic developed in previous works [1,2]. In the cyclohexane production process considered, we explore the e
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::b07d68db7038181bbb233727444a23b0
https://doi.org/10.1016/j.ijhydene.2014.10.042
https://doi.org/10.1016/j.ijhydene.2014.10.042
Publikováno v:
Industrial & Engineering Chemistry Research. 52:1698-1704
In this paper, we propose changes in the design of a cyclohexane production process, following a mass exchange design heuristic developed in a previous work (Ind. Eng. Chem. Res.2011, 50 (11), 6849-6859). In the study case considered, an optimal desi
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_dedup___::fccb1d727dde192ca6e3e3116bf9ffd4
https://doi.org/10.1021/ie302268p
https://doi.org/10.1021/ie302268p
Publikováno v:
Industrial & Engineering Chemistry Research. 50:12664-12677
This paper explores mass exchanging the outlet and inlet streams of a reactor, as a design heuristic within the hierarchical process design procedure by Douglas [AIChE J. 1985, 31 (3), 353–361 and Conceptual Design of Chemical Processes; McGraw–H
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::73e09015e5d74934ea738231e3a46dce
https://doi.org/10.1021/ie2013554
https://doi.org/10.1021/ie2013554
Publikováno v:
Industrial & Engineering Chemistry Research. 50:6849-6859
A hierarchical decision procedure is proposed for the synthesis of processes that are mass integrated to an existing industrial environment. The procedure takes the information about already instal...
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::e7fc40a0bf556a377ff8052bf4f5e102
https://doi.org/10.1021/ie102595x
https://doi.org/10.1021/ie102595x