diplomsko delo
Abstract
Glicerol je glavni stranski produkt v biodizelski industriji. Predstavlja kar
10 % mase nastalega biodizla. To je pripeljalo do znižanja cene glicerola, zaradi njegove
visoke porabe v svetovni proizvodnji. Glicerol lahko s pomočjo heterogenih
katalizatorjev pretvorimo v najbolj željene produkte, kot na primer akrolein, akrilno
kislino, dihidroksiaceton, hidroksiaceton, alil alcohol in druge kemikalije. Pred kratkim
so tem kemikalijam dodali še glicidol. Do zdaj se je zelo malo raziskovalo na področju
pridobivanja glicidola in glicerola. Enostopenjska sinteza poteka v kontinuirnem mikro
reaktorju s heterogenim katalizatorjem HZSM-5 zeolitom, modificiran pa je bil s
cezijevim nitratom CsNO3. V mojem diplomskem delu je bila izvedena optimizacija
omenjene reakcije s spreminjanjem treh parametrov; koncentracije modificiranega
cezijevega nitrata, temperature reakcije ter pretoka nosilnega plina in uplinjenega
vstopnega glicerola. Glede na dobljene rezultate, bi se lahko sčasoma cena glicidola
znižala, saj bi se reakcija s pomočjo teh optimizacij prenesla v industrijo.
Keywords
glicerol;glicidol;mikroreaktor;zeolit;heterogeni katalizator;diplomska dela;
Data
Language: |
Slovenian |
Year of publishing: |
2022 |
Typology: |
2.11 - Undergraduate Thesis |
Organization: |
UL FKKT - Faculty of Chemistry and Chemical Technology |
Publisher: |
[M. Atelšek] |
UDC: |
66.097(043.2) |
COBISS: |
127890947
|
Views: |
51 |
Downloads: |
18 |
Average score: |
0 (0 votes) |
Metadata: |
|
Other data
Secondary language: |
English |
Secondary title: |
Catalytic conversion of glycerol in a gas-phase |
Secondary abstract: |
Glycerol is the main byproduct in a biodiesel industry. It represents about 10
wt % of the biodiesel produced which led to a decrease of glycerol commercial price due
to its high abundance on the world market. Glycerol valorisation can be carried out in a
gas phase over heterogeneous catalysts, like acrolein, acrylic acid, dihydroxyacetone,
hydroxyacetone, allyl alcohol, and other chemicals. Recently glycidol was added to those
chemicals. Until now not a lot was studies in this area of glycidol production from
glycerol. This one step synthesis takes place in a packed bed micro reactor, packed with
a heterogenic catalyst HZSM-5 modified with CsNO3. In my work I was doing an
optimization of this reaction with studying three different parameters: mass
concentration, temperature and flow rate of carrier gas and feedstock glycerol. From the
results that I got, with time, this reaction could be transferred to industry with the help of
these optimizations. |
Secondary keywords: |
glycerol;glycidol;microreactor;zeolite;heterogeneous catalyst;Heterogena kataliza;Univerzitetna in visokošolska dela; |
Type (COBISS): |
Bachelor thesis/paper |
Study programme: |
1000372 |
Embargo end date (OpenAIRE): |
1970-01-01 |
Thesis comment: |
Univ. v Ljubljani, Fak. za kemijo in kemijsko tehnologijo, UNI Kemijsko inženirstvo |
Pages: |
37 str. |
ID: |
16391576 |