Temat: distillation - Katalog OPAC zbiorów

Skocz do pozycji: 1.

Tytuł:: Design and simulation of high purity biodiesel reactive distillation process
Autorzy:: Ali, Syed Sadiq
Asif, Mohammad
Basu, Avijit
Powiązania:: https://bibliotekanauki.pl/articles/779902.pdf
Data publikacji:: 2019
Wydawca:: Zachodniopomorski Uniwersytet Technologiczny w Szczecinie. Wydawnictwo Uczelniane ZUT w Szczecinie
Tematy:: biodiesel
reactive distillation
process simulator
recycle
purge
Opis:: Biodiesel is a promising energy substitute of fossil fuels since it is produced from renewable and biodegradable sources. In the present work, reactive distillation (RD) process is designed and simulated using Aspen Plus process simulator to produce biodiesel of high purity through esterification reaction. The simultaneous reaction and separation in same unit enhances the biodiesel yield and composition in RD process. Two flowsheets are proposed in present work. In the first flowsheet, the unreacted methanol is recycled back to reactive distillation column. Biodiesel with 99.5 mol% purity is obtained in product stream while the byproduct stream comprises 95.2 mol% water, which has to be treated further. In the second flowsheet, a part of methanol recycle is split and purged. In this case, the biodiesel composition in product stream is 99.7 mol% whereas water composition is 99.9 mol% in byproduct stream, which can be reused for other process without treatment.
Źródło:: Polish Journal of Chemical Technology; 2019, 21, 3; 1-7
1509-8117
1899-4741
Pojawia się w:: Polish Journal of Chemical Technology
Dostawca treści:: Biblioteka Nauki

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Skocz do pozycji: 2.

Tytuł:: Simulation and sensitivity analysis for biodiesel production in a reactive distillation column
Autorzy:: Agarwal, M.
Singh, K.
Chaurasia, S. P.
Powiązania:: https://bibliotekanauki.pl/articles/779118.pdf
Data publikacji:: 2012
Wydawca:: Zachodniopomorski Uniwersytet Technologiczny w Szczecinie. Wydawnictwo Uczelniane ZUT w Szczecinie
Tematy:: biodiesel
reactive distillation
modeling
simulation
transesterification
sensitivity analysis
Opis:: The conventional process for biodiesel production by transesterification is still expensive due to a need of high excess of alcohol required and its recovery by distillation. The use of a reactive distillation process can reduce the amount of alcohol in the feed stream as it works on a simultaneous reaction and separation. In the present study, a mathematical model has been developed for biodiesel production from triglycerides in a reactive distillation column, which has been validated with the reported data and CHEMCAD results. The effects of process parameters such as methanol to oil feed ratio, feed temperature, and reaction time have been investigated. The sensitivity analysis shows that yield of ester increases with methanol to oil ratio and number of stages, however, it decreases with fl ow rate. The MATLAB simulated results show that methanol to oil molar ratio of 5:1 produces 90% (by wt.) of methyl ester in a residence time of 4.7 minutes.
Źródło:: Polish Journal of Chemical Technology; 2012, 14, 3; 59-65
1509-8117
1899-4741
Pojawia się w:: Polish Journal of Chemical Technology
Dostawca treści:: Biblioteka Nauki

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Skocz do pozycji: 3.

Tytuł:: Determining the effect of oil after frying fish for the production of biofuels with a fractional composition of FAME
Autorzy:: Wcisło, G.
Pracuch, B.
Tomyuk, V.
Powiązania:: https://bibliotekanauki.pl/articles/411347.pdf
Data publikacji:: 2019
Wydawca:: Polska Akademia Nauk. Oddział w Lublinie PAN
Tematy:: biodiesel
FAME – Fatty Acid Methyl Esters
diesel engine
fractional composition
temperature distillation
Opis:: The aim of the study was to determine the impact of the fish frying process on the distillation properties of FAME and its mixtures with diesel fuel. The fish was fried at 160°C for 2 hours. Frying one serving lasted 6 minutes. The frying oil was a mixture of 50% (v/v) rapeseed oil and 50% (v/v) sunflower oil. The study showed that FAME biodiesel made from unused (pure) oil has similar distillation properties. The largest differences were observed for distillation temperatures of 85% and 100% and the final temperature of the distillation process. This may indicate a slightly lower purity of FAME produced from used cooking oil. In such a biofuel there may be more less volatile mono- and diglycerides or other chemicals that, e.g. after frying, remain in oil. It must be said, however, that they are not solid particles because they have been separated from the oil by filtration.
Źródło:: ECONTECHMOD : An International Quarterly Journal on Economics of Technology and Modelling Processes; 2019, 8, 3; 37-41
2084-5715
Pojawia się w:: ECONTECHMOD : An International Quarterly Journal on Economics of Technology and Modelling Processes
Dostawca treści:: Biblioteka Nauki

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Skocz do pozycji: 4.

Tytuł:: Determination of the impact of the type of animal fat used for production of biofuels on the fractional composition of AME
Autorzy:: Wcisło, G.
Labak, N.
Powiązania:: https://bibliotekanauki.pl/articles/410965.pdf
Data publikacji:: 2017
Wydawca:: Polska Akademia Nauk. Oddział w Lublinie PAN
Tematy:: biodiesel
AME
animal fat methyl esters
diesel engine
fractional composition
temperature distillation
estry metylowe tłuszczu zwierzęcego
silnik Diesla
skład frakcyjny
temperatura destylacji
Opis:: The aim of the study was to determine the impact of the frying process on the fractional composition of AME Biodiesel in comparison to the AME obtained from unused (fresh) animal fat. The fresh animal fat was divided into two portions. One was used for frying chips at 63°C for a period of 4 hours. The study showed the AME biodiesel produced from unused (pure) animal fat generally has better distillation properties. The temperatures at the start of distillation were similar for both of the AMEs. Within the 45-60% mid-range temperatures, the AME produced from the used cooking animal fat was characterized by higher distillation temperatures for the same volume of fuel. The largest differences were observed for the 85% and 95% distillation temperatures and the final temperature of the distillation process. This may testify to lower purity of the AME produced from the used cooking oil. In such a biofuel may consist less volatile mono-diglycerides or other chemicals which remain in the oil after frying. It must be said, though, these are not solid particles, as those were separated from the oil through filtration.
Źródło:: ECONTECHMOD : An International Quarterly Journal on Economics of Technology and Modelling Processes; 2017, 6, 1; 111-114
2084-5715
Pojawia się w:: ECONTECHMOD : An International Quarterly Journal on Economics of Technology and Modelling Processes
Dostawca treści:: Biblioteka Nauki

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Skocz do pozycji: 5.

Tytuł:: Determination of the impact of the type of corn oil used for production of biofuels on the fractional composition of CME
Określenie wpływu rodzaju użytego oleju kukurydzianego do produkcji biopaliw na skład frakcyjny CME
Autorzy:: Wcisło, G.
Labak, N.
Powiązania:: https://bibliotekanauki.pl/articles/134033.pdf
Data publikacji:: 2015
Wydawca:: Polskie Towarzystwo Naukowe Silników Spalinowych
Tematy:: biodiesel
CME
Corn Methyl Esters
corn oil
diesel engine ZS
fractional composition
temperature distillation
estry metylowe oleju kukurydzianego
olej kukurydziany
silnik o zapłonie samoczynnym ZS
skład frakcyjny
temperatura destylacji
Opis:: The aim of the study was to determine the impact of the frying process on the fractional composition of CME Biodiesel in comparison to the CME obtained from unused (fresh) corn oil. The freshly pressed corn oil was divided into two portions. One was used for frying chips at 493K for a period of 12 hours. The study showed the CME biodiesel produced from unused (pure) corn oil generally has better distillation properties. The temperatures at the start of distillation were similar for both of the CMEs. Within the 40-65% mid-range temperatures, the CME produced from the used cooking corn oil was characterized by higher distillation temperatures for the same volume of fuel. The largest differences were observed for the 90% and 95% distillation temperatures and the final temperature of the distillation process. This may testify to lower purity of the CME produced from the used cooking oil. In such a biofuel there may be more less volatile mono- and diglycerides or other chemicals which e.g. remain in the oil after frying.
Celem badań było określenie wpływu procesu smażenia na skład frakcyjny biodiesla CME w stosunku do CME uzyskanego z niezużytego (świeżego) oleju kukurydzianego. Świeżo wytłoczony olej z kukurydziany podzielono na dwie porcje. Jedną z nich wykorzystano do smażenia frytek w temperaturze do 493K przez łączny okres 12 godz. Przeprowadzone badania pokazały, że biodiesel CME wytworzony z niezużytego (czystego) oleju kukurydzianego charakteryzował się generalnie lepszymi własnościami destylacyjnymi. Przy czym temperatury początku destylacji były zbliżone dla obydwu CME. Dla temperatur ze środkowego zakresu 40 do 65% CME wytworzony z posmażalniczego oleju kukurydzianego charakteryzował się wyższymi temperaturami destylacji tej samej objętości paliwa. Największe różnice odnotowano dla temperatur oddestylowania 90 % i 95% oraz końca destylacji. Może to świadczyć o mniejszej czystości CME uzyskanego ze zużytego oleju. W takim biopaliwie może znajdować się więcej mało lotnych mono i di-glicerydów lub innych związków, które np. pozostały w oleju po procesie smażenia frytek.
Źródło:: Combustion Engines; 2015, 54, 3; 1082-1087
2300-9896
2658-1442
Pojawia się w:: Combustion Engines
Dostawca treści:: Biblioteka Nauki

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