the Initiation of Direct Contact Heat Exchanger Addition at the Evaporation Station of the X Sugar Mill
DOI:
https://doi.org/10.35261/barometer.v9i2.10205Abstract
White crystal sugar is one of the plantation commodities that is widely produced because it is widely consumed by the people of Indonesia. White crystalline sugar at Sugar X Factory is made from sugarcane sap which has gone through the refining stage into clear sap and then concentrated using an evaporator to become thick sap, where thick sap will become white crystalline sugar after crystallization. In the process of converting clear sap into viscous sap, it requires quite a lot of steam in the evaporator, causing the used steam in the Sugar Factory to be consumed more by the Evaporation Station. In fact, in the Sugar X factory, many steam has not been able to thicken the clear sap to the maximum due to the considerable workload. This is because the incoming temperature is very low, so the temperature must be raised in order to reach the flash point to evaporate. A direct contact heat exchanger equipment needs to be installed before entering the evaporator at the Evaporation Station of the X Sugar Factory. The purpose of this research is to obtain a direct contact heat exchanger or DCHE design which will then be installed at the X Sugar Factory Evaporation Station. To obtain the desired direct contact heat exchanger design, actual data, literature data, and assumption data are needed. Based on calculations, this DCHE has an outer diameter of 1,062 meters with a height of 8,628 meters. Based on calculations, this DCHE has an outer diameter of 1,062 meters with a height of 8,628 meters. After calculation, it was found that this tool can save used steam consumption as much as 14,467 tons / hour and can increase the capacity of the tool from 5,622 TCD to 6,371 TCD, so that this equipment is considered feasible in terms of economy and use for use as a preheater before entering the evaporator of the Evaporation Station.
Downloads
References
N. Muhammad., (2024, Januari 20). Jawa Timur jadi Produsen Gula Terbesar Nasional [Online]. Available: Jawa Timur Jadi Produsen Gula Terbesar Nasional 2022 (katadata.co.id)
W. F. S. Pratama., (2024, Januari 20). Laporan Praktik Kerja Lapang PTPN X PG Ngadirejo Kediri [Online]. Available: https://repository.upnjatim.ac.id/19659/3/19031010183.-bab2.pdf.
S. Wiyono, E. Erwin, and S. Abdullah, “Pengolahan Air Nira Dengan Vacuum Evaporasi Menjadi Gula Aren Cair,” Tek. J. Tek., vol. 8, no. 2, p. 122, 2021, doi: 10.35449/teknika.v8i2.196.
R. J. Prabaswara, S. Rulianah, C. Sindhuwati, and R. Raharjo, “Evaluasi Pressure Drop Heat Exchanger-03 Pada Crude Distillation Unit Ppsdm Migas Cepu,” DISTILAT J. Teknol. Separasi, vol. 7, no. 2, pp. 505–513, 2023, doi: 10.33795/distilat.v7i2.287.
T. Nomura, M. Tsubota, N. Okinaka, and T. Akiyama, “Improvement on heat release performance of direct-contact heat exchanger using phase change material for recovery of low temperature exhaust heat,” ISIJ Int., vol. 55, no. 2, pp. 441–447, 2015, doi: 10.2355/isijinternational.55.441.
T. Lemenand, C. Durandal, D. Della Valle, and H. Peerhossaini, “Turbulent direct-contact heat transfer between two immiscible fluids,” Int. J. Therm. Sci., vol. 49, no. 10, pp. 1886–1898, 2010, doi: 10.1016/j.ijthermalsci.2010.05.014.
D. I. Pg and K. Agung, “Desain Direct Contact Heat Exchanger (Dche) Pada Unit Masakan Defekasi - Remelt - Karbonatasi (Drk) Di Pg Kebon Agung Malang,” Distilat J. Teknol. Separasi, vol. 8, no. 2, pp. 385–393, 2022, doi: 10.33795/distilat.v8i2.380.
E. Hugot, Handbook of Cane Sugar Engineering, Third. Elsevier Ltd, 1986.
V.E. Baikow, Manufacture and Refining of Raw Cane Sugar. Elsevier Ltd, 1967.
S. Alluri, (2023, November 5). Direct Contact Heater (DCH) Design Calculation. Available: http://www.sugarprocesstech.com/direct-contact-heater-design/
W. Du, H. Wang, and L. Cheng, “Effects of Shape and Quantity of Helical Baffle on the Shell-side Heat Transfer and Flow Performance of Heat Exchangers *,” Chinese J. Chem. Eng., vol. 22, no. 3, pp. 243–251, 2014, doi: 10.1016/S1004-9541(14)60041-0.
L. E. Brownell and E. H. Young, “Brownell Process Equipment Design Handb.pdf.” 1959.
H. Ameur, “Effect of the baffle inclination on the flow and thermal fields in channel heat exchangers,” Results Eng., vol. 3, p. 100021, 2019, doi: 10.1016/j.rineng.2019.100021.
R. Thundil Karuppa Raj and S. Ganne, “Shell side numerical analysis of a shell and tube heat exchanger considering the effects of baffle inclination angle on fluid flow,” Therm. Sci., vol. 16, no. 4, pp. 1165–1174, 2012, doi: 10.2298/TSCI110330118R.
Ley 25.632, “済無No Title No Title No Title,” pp. 1–9, 2002.
F. B. Sulistiono and R. Trisno, “Pengaruh Liquid Suction Heat Exchanger Terhadap Kinerja Sistem Pendingin Pada Mesin Portable Chiller,” J. Rekayasa Mesin, vol. 14, no. 3, pp. 845–855, 2023, doi: 10.21776/jrm.v14i3.1368.
E. Pada et al., “Analisis Pengaruh Tekanan Uap Bekas Terhadap Karakteristik Perpindahan Panas Sistem Evaporator 5 Efek Pada Pg Kedawoeng, Pasuruan,” Distilat J. Teknol. Separasi, vol. 8, no. 1, pp. 185–195, 2022, doi: 10.33795/distilat.v8i1.320.
J. Sumarjo, R. D. Anjani, and A. Santosa, “Perencanaan alat penukar kalor untuk pengering kain dengan memanfaatkan energi panas dari gas buang mesin diesel 1,” vol. 3, no. 1, pp. 105–112, 2018.
S. Vivek et al., “Performance evaluation of simple DPHX with helical baffles in annulus side,” J. Phys. Conf. Ser., vol. 1921, no. 1, 2021, doi: 10.1088/1742-6596/1921/1/012090.
H. Sadighi Dizaji, S. Jafarmadar, and F. Mobadersani, “Experimental studies on heat transfer and pressure drop characteristics for new arrangements of corrugated tubes in a double pipe heat exchanger,” Int. J. Therm. Sci., vol. 96, pp. 211–220, 2015, doi: 10.1016/j.ijthermalsci.2015.05.009.