Gustine i viskoznosti binarnih sistema sa N,N-dimetilanilinom i tetra etilen glikolom dimetil etrom ili N-metil-2-pyrolidonom, kao potencijalni rastvarači za procese odsumporavanja dimnih gasova

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Nikola Živković http://orcid.org/0000-0003-3399-1229 Emila Živković http://orcid.org/0000-0001-5843-8230 Mirjana Kijevčanin http://orcid.org/0000-0001-7126-3965

Apstrakt

Oksidi sumpora emituju se kao jedan od proizvoda u procesu sagorevanja čvrstih fosilnih goriva u termoelektranama, posebno kolubarskog i kostolačkog lignita u Republici Srbiji. Da bi se smanjio nivo emisije indirektnih gasova staklene bašte (GHG) iz stacionarnih izvora, neizbežna je primena tehnologije odsumporavanja dimnih gasova (FGD). Pored klasičnog krečnjačkog postupka, sve su češći tehnološki postupci zasnovani na fizičkoj ili hemijskoj apsorpciji sumpornih oksida u rastvaraču i njegovoj termičkoj regeneraciji. Da bi se pravilno dizajnirao i optimizovao proces, važno je precizno odrediti termofizička svojstva čistih komponenti i njihovih smeša.


U radu su prikazani rezultati određivanja gustine i viskoziteta dve binarne smeše, N,N-dimetilanilin (N,N-DMA) + tetra etilen glikol dimetil etar (TEGDME) i N,N-dimetilanilin (N,N-DMA) + N-metil-2-pirolidon (NMP). Merenja su vršena pomoću gustinomera Anton Paar DMA 5000 i Stabinger viskozimetra Anton Paar SVM 3000/G2, na atmosferskom pritisku. Dobijeni eksperimentalni rezultati su prikazani kao funkcija temperature i molskog udela N,N-DMA.


N,N-DMA pripada grupi amina, a korišćen je kao sorbent za prečišćavanje dimnih gasova u procesima sa termičkom regeneracijom (CANSOLV, Sulphidine i ASARCO procesi). Druga dva organska rastvarača su TEGDME i NMP. Posebna pažnja je posvećena NMP-u zbog niske cene i niskog viskoziteta, sa svojim povoljnim svojstvima, što ga čini konkurentnim kao rastvarač za FGD. TEGDME je polarni rastvarač, ali nije selektivan ka SO2 i druge gasovite komponente, pa je NMP predložen kao alternativno rešenje. Regenerativni proces za uklanjanje SO2, sa TEGDME, već je našao komercijalnu primenu (Solinox proces). NMP se već industrijski koristi kao rastvarač u Lurgi's Purisol procesu, zbog svoje prirode za selektivno odsumporavanje dimnih gasova.

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Kako citirati
ŽIVKOVIĆ, Nikola; ŽIVKOVIĆ, Emila; KIJEVČANIN, Mirjana. Gustine i viskoznosti binarnih sistema sa N,N-dimetilanilinom i tetra etilen glikolom dimetil etrom ili N-metil-2-pyrolidonom, kao potencijalni rastvarači za procese odsumporavanja dimnih gasova. Zbornik Međunarodnog kongresa o procesnoj industriji – Procesing, [S.l.], v. 37, n. 1, p. 167-176, june 2024. Dostupno na: <https://izdanja.smeits.rs/index.php/ptk/article/view/8058>. Datum pristupa: 07 dec. 2024 doi: https://doi.org/10.24094/ptk.024.167.
Sekcija
Inženjerstvo životne sredine i održivi razvoj

Reference

[1] Arthur L. Kohl, Richard B. Nielsen, Gas Purification, 5th edition, Gulf Publishing Compa-ny, Houston, Texas, United States (1997),
[2] *** Flue Gas Desulfurization (Acid Gas Removal) Systems, Lesson 9, United States Envi-ronmental Protection Agency, http://www.epa.gov (18.06.2015),
[3] R. K. Srivastava, W. Jozewicz, C. Singer, SO2 Scrubbing Technologies: A Review, Envi-ron. Prog., 20 (2001) 219-228,
[4] N.V. Živković, S.P. Šerbanović, E.M. Živković, M.Lj. Kijevčanin, P.Lj. Stefanović, Wet Flue Gas Desulphurisation Procedures And Relevant Solvent Thermophysical Properties De-termination, Chemical Industry, 68 (2014) 491-500,
[5] *** Wet Gas Desulfurization (FGD) Systems, Advanced Technology For Maximum SO2 Removal, Babcock & Wilcox Power Generation Group, www.babcock.com,
[6] Sporer J., The Linde Solinox Process: Gypsum-free flue-gas desulphurization, Gas Sep. & Purif., 6 (1992) 133-140,
[7] Heisel M., Belloni A., Options available in the Solinox vent gas purification process, Gas Sep. & Purif., 5 (1991) 111-113,
[8] *** The CANSOLV SO2 Scrubbing System, A Shell Company, Cansolv – Gas Absorption Solutions, http://www.shell.com/global/products-services/solutions-for-businesses/globalsolutions/shell-cansolv/shell-cansolv-solutions/so2-capture.html (18.06.2015),
[9] M.Heisel, A. Belloni, Options available in the Solinox vent gas purification process, Gas Sep. & Purif., 5 (1991) 111-113,
[10] J. Sporer, The Linde Solinox Process: Gypsum-free flue-gas desulphurization, Gas Sep. & Purif., 6 (1992) 133-140,
[11] Živković N. V., Šerbanović S. P., Kijevčanin M. Lj., Živković E. M. „Volumetric and Vis-cosimetric Behavior of Binary Systems 2-Butanol + PEG 200, + PEG 400, + Tetraethylene Glycol Dimethyl Ether, and + N-Methyl-2-pyrrolidone“, Journal of Chemical Engineering Data, 58 (12), pp 3332-3341, Print Edition ISSN: 0021-9568, Web Edition ISSN: 1520-5134, DOI 10.1021/je400486p
[12] N. Živković, S. Šerbanović, M. Kijevčanin, E. Živković, “Volumetric Properties, Viscosi-ties, and Refractive Indicies of the Binary Systems 1-Butanol+PEG 200, + PEG 400, and + TEGDME“, International Journal of Thermophysics, 34(6) (2013), 1002-1020, ISSN: 0195-928X (Print) 1572-9567 (Online), DOI 10.1007/s10765-013-1469-0,
[13] E.M. Živković, N.V. Živković, D.M. Majstorović, I.R. Radović, A.M. Stanimirović, J.D. Jovanović, M.Lj. Kijevčanin, Binary mixture of N,N-dimethylaniline and polyethylene gly-col 400 as potential solvent for regenerative flue gas desulfurization processes, VII Interna-tional Conference Industrial Engineering And Environmental Protection 2017 (IIZS 2017), University of Novi Sad, Technical Faculty “Mihajlo Pupin”, Zrenjanin, Serbia, October 12-13th, 2017, Proceedings, pp. 203-208, (ISBN: 978-86-7672-303-4),
[14] V. Pandiyan, S.L. Oswal, P. Vasantharani, Thermodynamic and acoustic properties of bi-nary mixtures of ethers. IV. Diisopropyl ether or oxolane with N,N-dimethylaniline or N,N-diethylaniline at 303.15, 313.15 and 323.15 K, Thermochim. Acta, 518 (2011) 36–46.
[15] M. Kondaiah, D. Sravana Kumar, K. Sreekanth, D. Krishna Rao, Densities and Viscosi-ties of Binary Mixtures of Propanoic Acid with N,N-Dimethylaniline and N,N-Diethylaniline at T = (303.15, 313.15, and 323.15) K, J. Chem Eng. Data, 57 (2012) 352–357,
[16] A.G. Oskoei, N. Safaei, J. Ghasemi, Densities and Viscosities for Binary and Ternary Mix-tures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T = (283.15 to 343.15) K, J. Chem Eng. Data, 53 (2008)343–349,
[17] A. Pal, G. Dass, A. Kumar, Excess Molar Volumes, Viscosities, and Refractive Indices of Tetraethylene Glycol Dimethyl Ether + Dimethyl Carbonate, +Diethyl Carbonate, and + Pro-pylene Carbonate at 298.15 K,J. Chem Eng. Data, 44 (1999) 2-5,
[18] J.N. Real, T.P. Iglesias, S.M. Pereira, M.A. Rivas, Analysis of temperature dependence of some physical properties of (n-nonane + tetraethylene glycol dimethyl ether), J. Chem. Thermodyn., 34 (2002) 1029-1043,
[19] M.E. Ferreyra de Ruiz Holgado, R.C. de Schaefer, L.E. Arancibia, Densities and Viscosi-ties of Binary Mixtures of Polyethylene Glycol 350 Monomethyl Ether with n-Butanol and n-Pentanol and Tetraethylene Glycol Dimethyl Ethers with n-Propanol, n-Butanol, and n-Pentanol from 278.15 K to 318.15 K, J. Chem Eng. Data, 47 (2002) 144-148,
[20] F.J. Carmona, F.J. Arroyo, I.D. de la Fuente, J.A. Gonzales, J.C. Cobos, Excess Molar Volumes of Methanol or Ethanol + n-Polyethers at 298.15 K, Can. J. Chem., 77 (1999) 1608-1616,
[21] A. Henni, J.J. Hromek, P. Tontiwachwuthikul, A. Chakma, Volumetric Properties and Viscosities for Aqueous N-Methyl-2-pyrrolidone Solutions from 25 oC to 70 oC, J. Chem Eng. Data, 49 (2004) 231-234,
[22] D.D. McDonald, D. Dunay, G. Hanlon, J.B. Hyne, Properties of the n-methyl-2-pyrrolidinone-water system, Can. J. Chem. Eng., 49 (1971) 420-423,
[23] J. George, N.V. Sastry, Densities, Viscosities, Speeds of Sound, and Relative Permittivities for Water+Cyclic Amides (2-Pyrrolidinone, 1-Methyl-2-pyrrolidinone, and 1-Vinyl-2-pyrrolidinone) at Different Temperatures, J. Chem Eng. Data, 49 (2004) 235−242,
[24] Y.P. Handa, G.C. Benson, Volume changes on mixing two liquids: A review of the experi-mental techniques and the literature data, Fluid Phase Equilib., 3 (1979) 185-249.
[25] D. Bajić, Eksperimentalno određivanje i modelovanje viskoznosti, gustine i indeksa refrakci-je binarnih smeša sa alkoholima i tečnim PEG, master rad, Univerzitet u Beogradu, Tehnološko-Metalurški fakultet, Beograd 2010.
[26] B. Ðorđevic, V. Valent, S. Šerbanovic, Termodinamika sa termotehnikom, Tehnološko-Metalurški Fakultet, Beograd, 2003.
[27] O. Redlich, A. T. Kister, Algebraic Representation of Thermodynamic Properties and the Classification of Solutions, Ind. Eng. Chem., 40 (1948) 345-348.