ANALISA ENERGI DAN EKSERGI PADA PENGERINGAN TEPUNG TAPIOKA MENGGUNAKAN PENGERING KONTINYU UNGGUN FLUIDISASI GETAR

Suherman Suherman; Rona Trisnaningtyas

doi:10.14710/reaktor.16.1.24-31

DOI: https://doi.org/10.14710/reaktor.16.1.24-31

ANALISA ENERGI DAN EKSERGI PADA PENGERINGAN TEPUNG TAPIOKA MENGGUNAKAN PENGERING KONTINYU UNGGUN FLUIDISASI GETAR

*Suherman Suherman - Jurusan Teknik Kimia, Fakultas Teknik Universitas Diponegoro, Indonesia

Rona Trisnaningtyas - Jurusan Teknik Kimia, Fakultas Teknik Universitas Diponegoro

Received: 9 Apr 2015; Published: 15 May 2016.

BibTex Citation Data :

@article{Reaktor8413,
    author = {Suherman Suherman and Rona Trisnaningtyas},
    title = {ANALISA ENERGI DAN EKSERGI PADA PENGERINGAN TEPUNG TAPIOKA MENGGUNAKAN PENGERING KONTINYU UNGGUN FLUIDISASI GETAR},
    journal = {Reaktor},
  volume = {16},
    number = {1},
    year = {2016},
    keywords = {Analisa energi dan eksergi, pati tapioka, pengeringan kontinyu, unggun fluidisasi getar},
    abstract = {  Energy and exergy analysis of cassava starch drying in continuous vibrated fluidized bed dryer were carried out to assess the performance of the system in terms of energy utilization ratio, energy efficiency, exergy inflow and outflow, exergy loss, and exergetic efficiency. The results showed cassava starch has starch content 87%, degree of whiteness 95%, negative fiber content, sperichal granula with average diameter12.32 μm, orthorhombic crystal structure and crystal size 47.467 nm . Energy utilization and energy utilization ratio increased from 0.08 to 0.20 J/s and 0.35 to 0.4 as the drying temperature  increased from 50 to 70  o C. Energy efficiency increased from 13.80 % to 23.31 %, while exergy inflow, outflow, and losses increased from 4.701 to 14.678, 2.277 to 6.344, and 2.424 to 8.334 J/s respectively in the above temperature range. Exergetic efficiency decreased with increase in drying air temperature, while exergetic improvement potential increased with increased drying air temperature.     Keywords :  Cassava starch, continuous drying, energy and exergy analysis, vibrated fluidized bed            Abstrak     Analisis energi dan eksergi pengeringan pati tapioka menggunakan pengering kontinu unggun fluidisasi getar, telah dilakukan untuk menilai kinerja sistem dalam bentuk utilisasi energi, efisiensi energi, eksergi masuk dan keluar, eksergi hilang dan efisiensi eksergi. Hasil analisis pati memiliki kandungan starch 87%, tingkat keputihan 95%, kandungan serat negatif, bentuk partikel granular spherical dengan diameter 12,32 μm, struktur kristal orthorhombic dan ukuran kristal sebesar 47,467 nm. Peningkatan suhu pengering dari 50 menjadi 70  0 C akan meningkatkan utilisasi energi dan rasio utilisasi energi dari 0,08 menjadi 0,20 J/s dan 0,35 menjadi 0,4. Efisiensi energi meningkat dari   13,80% hingga 23,31%, sedangkan eksergi masuk dan keluar, eksergi hilang meningkat dari 4,701 menjadi 14,678, 2,277 menjadi 6,344, dan 2,424 menjadi 8,334 J/s. Efisiensi eksergi menurun dengan naiknya suhu sedangkan potensi pengembangan eksergi meningkat dengan naiknya suhu.     Kata kunci : . Analisis energi dan eksergi, pati tapioka, pengeringan kontinu, unggun fluidisasi getar     },
   issn = {2407-5973},   pages = {24--31}  doi = {10.14710/reaktor.16.1.24-31},
    url = {https://ejournal.undip.ac.id/index.php/reaktor/article/view/8413}
}

Citation Format:

Abstract

Energy and exergy analysis of cassava starch drying in continuous vibrated fluidized bed dryer were carried out to assess the performance of the system in terms of energy utilization ratio, energy efficiency, exergy inflow and outflow, exergy loss, and exergetic efficiency. The results showed cassava starch has starch content 87%, degree of whiteness 95%, negative fiber content, sperichal granula with average diameter12.32 μm, orthorhombic crystal structure and crystal size 47.467 nm . Energy utilization and energy utilization ratio increased from 0.08 to 0.20 J/s and 0.35 to 0.4 as the drying temperature increased from 50 to 70 ^oC. Energy efficiency increased from 13.80 % to 23.31 %, while exergy inflow, outflow, and losses increased from 4.701 to 14.678, 2.277 to 6.344, and 2.424 to 8.334 J/s respectively in the above temperature range. Exergetic efficiency decreased with increase in drying air temperature, while exergetic improvement potential increased with increased drying air temperature.

Keywords: Cassava starch, continuous drying, energy and exergy analysis, vibrated fluidized bed

Abstrak

Analisis energi dan eksergi pengeringan pati tapioka menggunakan pengering kontinu unggun fluidisasi getar, telah dilakukan untuk menilai kinerja sistem dalam bentuk utilisasi energi, efisiensi energi, eksergi masuk dan keluar, eksergi hilang dan efisiensi eksergi. Hasil analisis pati memiliki kandungan starch 87%, tingkat keputihan 95%, kandungan serat negatif, bentuk partikel granular spherical dengan diameter 12,32 μm, struktur kristal orthorhombic dan ukuran kristal sebesar 47,467 nm. Peningkatan suhu pengering dari 50 menjadi 70 ⁰C akan meningkatkan utilisasi energi dan rasio utilisasi energi dari 0,08 menjadi 0,20 J/s dan 0,35 menjadi 0,4. Efisiensi energi meningkat dari 13,80% hingga 23,31%, sedangkan eksergi masuk dan keluar, eksergi hilang meningkat dari 4,701 menjadi 14,678, 2,277 menjadi 6,344, dan 2,424 menjadi 8,334 J/s. Efisiensi eksergi menurun dengan naiknya suhu sedangkan potensi pengembangan eksergi meningkat dengan naiknya suhu.

Kata kunci:. Analisis energi dan eksergi, pati tapioka, pengeringan kontinu, unggun fluidisasi getar

Fulltext View|Download

Keywords: Analisa energi dan eksergi, pati tapioka, pengeringan kontinyu, unggun fluidisasi getar

Funding: Kemendikbud

Article Metrics:

Article Info

Section: Research Article

Language : IND

In Volume 16 No.1 Maret 2016

Recent articles

Front Matter Reaktor Vol 16 No. 1 Maret 2016 MODIFIED STARCH OF AMORPHOPHALLUSCAMPANULATUS AS A NOVEL ADSORBENT FOR WATERADSORPTION Pemanfaatan Limbah Pretreatment Dalam Produksi Bioetanol Dari Lignoselulosa Untuk Me-Recovery Fine Chemicals Dengan Proses Pirolisa AMOKSIMASI SIKLOHEKSANON DENGAN KATALIS MoO3/TS-1 MENGGUNAKAN HIDROGEN PEROKSIDA SEBAGAI AGEN PENGOKSIDASI Back Matter Reaktor Vol 16 No. 1 Maret 2016 More recent articles

Most cited articles

AKTIVASI ZEOLIT ALAM SEBAGAI ADSORBEN PADA ALAT PENGERING BERSUHU RENDAH Fabrication and characterization of polyimide/ polyethersulfone-fumed silica mixed matrix membrane for gas separation Peningkatan Produksi Gula Pereduksi dari Tandan Kosong Kelapa Sawit dengan Praperlakuan Asam Organik pada Reaktor Bertekanan PREPARASI KARBON TEREMBAN OKSIDA COBALT DARI LIMBAH KULIT MANGGIS SEBAGAI ADSORBEN PENJERAP ETILEN UNTUK PENGAWETAN BUAH THE INFLUENCES OF NATURAL GAS IMPURITIES TO THE SURFACE TENSION OF BLENDED PIPERAZINE-N-METHYLDIETHANOLAMINE (MDEA) SOLUTION More cited articles

Aghbashlo M., MH Kianmehr, A Arabhosseini, (2009), Performance analysis of drying carrot slice in a semi-industrial continuous band dryer, Food Eng., 91. 99-108
Aghbashlo M., MH Kianmehr, HS Akhijahani H., (2008), Influence of drying conditions on the effective moisture diffusivity, energy of activation, energy of activation and energy consumption during the thin-layer drying of berberis fruit (Berberidaceae), Energy Convers. Manage., 49(10). 2865-71
Akbulut, A., A. Durmus, (2010), Energy and exergy analysis of thin layer drying of mulberry in a forced solar dryer, Energy, 35. 1754-1763
Akpinar EK., (2005), Energy and exergy analyses of drying of eggplant slices in a cyclone type dryer, J. Mech. Sci. Tech., 19(2). 692-703
Akpinar EK., Midilli A., Bicer Y., (2005), Energy and exergy of potato drying process via cyclone type dryer, Energy Convers. Manage., 46. 2530-52
Assari, MR., HB. Tabrizi, E. Najafpour, (2013), Energy and exergy analysis of fluidized bed dryer based on two-fluid modeling, Int. J. Thermal Sci., 64. 213-219
Aviara NA, Igbeka JC, Nwokocha LM. (2010), Effect of drying temperature on physicochemical properties of cassava starch, Int. Agrophysics (24) 219-225
Aviara NA., LN. Onuoha, OE. Falola, JC. Igbeka (2014), Energy and exergy analysis of native cassava starch drying in a tray dryer, Energy, 73. 809-817
Boukadoum, AB, A. Benzaout, (2011), Energy and exergy analysis of solar drying process of mint, Energy Procedia, 6. 583-591
Colak N., A. Hepbasli, (2007), Performance analysis of drying of green olive in a tray dryer, J. Food Eng., 80(4). 1188-93
Corzo, O., N. Bracho, A. Vásquez, A. Pereira, (2008), Energy and exergy analysis of thin layer drying of coroba slices, J. Food Eng., 86. 151-161
Dincer, I., (2011), Exergy as a potential tool for sustainable drying system, Sustain Cities Soc., 1. 91-6
Dincer, I., AZ. Sahin, (2004), A new model for thermodynamics analysis of a drying process, Int. J. Heat Mass Transfer, 47. 645-52
Fudholi, A., K. Sopian, MY. Othman, MH Ruslan, (2014), Energy and exergy analyses of solar drying system of red seaweed, Energy and Buildings 68, 121–129
Hepbasli A., Z. Erbay, N. Colak, EH. Kuzgunkaya, F., Icier, (2010), An exergetic performance assessment of three different food driers, Proceedings of the Institution of Mech. Eng., Part A : J. Power Energy, 224 (1). 1-12
Karaguzel I., E. Tekin, A. Topuz, (2012), Energy and exergy analysis of fluidized bed drying of chickpea and bean, Sci. Res. Essays, 7(46), pp. 3961-3973,
Karimi F., S. Rafiee, (2012), Optimization of an air drying process for Artemisia absinthium leaves using response surface and artificial neural network models, J. Taiwan Ins. Chem. Eng., 43(1). 29-39
Midilli A., H. Kucuk, (2003), Energy and exergy analysis of solar drying process of pistachio, Energy, 28 (6). 539-56
Nazghelichi T., MH. Kianmehr, M. Aghbashlo, (2010), Thermodynamic analysis of fluidized bed drying of carrot cubes, Energy, 35. 4697-4684
Ocal C, (2013), Drying of natural zeolite powders in vibrated fluidized beds, Master Theses, Middle East Technical University
Palzer S., (2007), Drying of wet agglomeration in a continuous fluid bed : Influence of residence time, air temperature and air flowrate on the drying kinetics and the ammount of oversize particles, Chem. Eng. Sci., 62. 463-470
Sarker, M.S.H., MN. Ibrahim, NA Aziz, MS Punan, (2015), Energy and exergy analysis of industrial fluidized bed drying of paddy, Energy, 84, 131-138
Smail M., (2011), Drying kinetics of olive pomace in a fluidized bed dryer, Energy Convers. Manage., 52. 1644-1649
Stakic M., T. Urosevic, (2011), Experimental study and simulation of vibrated fluidized bed drying, Chem. Eng. Process., 50. 428-437
Tonukari, NJ., (2004), Cassava and the future of starch, Electron. J. Biotech., 7 (1). 5-8
Venkantesh, R. Deiva, M. Grmela, J. Chaouki, (1998), Simulations of vibrated fine powders, Powder Technol., 100. 211-222
Yang X, Y. Zhao, Z. Luo, S. Song, C. Duan, L. Dong, (2013), Fine coal dry cleaning using a vibrated gas-fluidized bed, Fuel Process. Technol., 106. 338-343
Zhao P., Y. Zhao, Z. Chen, Z. Luo, (2015), Dry cleaning of fine lignite in vibrated gas-fluidized bed : Segregation characteristics, Fuel, 142. 274-282

Last update:

Proceedings of the 3rd International Conference on Experimental and Computational Mechanics in Engineering
Thaharul Fikri, Ahmad Syuhada, Razali Thaib. Lecture Notes in Mechanical Engineering, 2023. doi: 10.1007/978-981-19-3629-6_25
Energy and exergy analysis economic of continuous vibrating fluidized bed drying on celery drying
S U Handayani, I S Atmanto, F T Putri, S Fujiwara. Journal of Physics: Conference Series, 1524 (1), 2020. doi: 10.1088/1742-6596/1524/1/012030
Performance Evaluation of Pneumatic Dryer for Aren (Arenga piñata) Flour
Suherman Suherman, Nur Hidayati, A.C. Kumoro, Hadiyanto, S.A. Roces, L. Yung, X. Rong, A.W. Lothongkum, M.T. Phong, M.A. Hussain, W.R.W. Daud, P.T.S. Nam. MATEC Web of Conferences, 156 , 2018. doi: 10.1051/matecconf/201815605023

Last update: 2025-01-22 08:21:22

No citation recorded.

In order for REAKTOR to publish and disseminate research articles, we need non-exclusive publishing rights (transferred from the author(s) to the publisher). This is determined by a publishing agreement between the Author(s) and REAKTOR. This agreement deals with transferring or licensing the publishing copyright to REAKTOR while Authors still retain significant rights to use and share their published articles. REAKTOR supports the need for authors to share, disseminate, and maximize the impact of their research and these rights in any databases.

As a journal author, you have the right to use your article for many purposes, including by your employing institute or company. These Author rights can be exercised without the need to obtain specific permission. Authors publishing in BCREC journals have wide rights to use their works for teaching and scholarly purposes without needing to seek permission, including, but not limited to:

use for classroom teaching by the Author or the Author's institution and presentation at a meeting or conference and distributing copies to attendees;
use for internal training by the author's company;
distribution to colleagues for their research use;
use in a subsequent compilation of the author's works;
inclusion in a thesis or dissertation;
reuse of portions or extracts from the article in other works (with full acknowledgment of the final article);
preparation of derivative works (other than commercial purposes) (with full acknowledgment of the final article);
voluntary posting on open websites operated by the author or the author’s institution for scholarly purposes,

(but it should follow the open access license of Creative Common CC-by-SA License).

Authors/Readers/Third Parties can copy and redistribute the material in any medium or format and remix, transform, and build upon the material for any purpose, even commercially. Still, they must give appropriate credit (the name of the creator and attribution parties (authors detail information), a copyright notice, an open access license notice, a disclaimer notice, and a link to the material), provide a link to the license, and indicate if changes were made (Publisher indicates the modification of the material (if any).

Authors/Readers/Third Parties can read, print and download, redistribute or republish the article (e.g., display in a repository), translate the article, download for text and data mining purposes, reuse portions or extracts from the article in other works, sell or re-use for commercial purposes, remix, transform, or build upon the material, they must distribute their contributions under the same license as the original Creative Commons Attribution-ShareAlike (CC BY-SA).