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dc.contributor.authorYulianto, Sulis
dc.contributor.authorMaghfurah, Fadwah
dc.contributor.authorQadri, Munzir
dc.date.accessioned2014-12-02T07:34:52Z
dc.date.available2014-12-02T07:34:52Z
dc.date.issued2014-12-04
dc.identifier.citation[1] Ramesh K. Sahah and Dusan P Sekulic 2003. Fundamentals of Heat ExchengerDesing. John Wiley & Son, INC. Hoboken, New Jersey. [2] Ricahard. C. Byrne. 2000. Standard of the Turbular Excharnger Manufactures Association, standards of the Turbular Exchanger Manufacture Assocition, INC. New York,. [3] Epstein, N. 1978. Fouling in Heat Exchangers, Heat Transfer Engineering, vol 6, New York,. [4] Keith Escoe, A., Mechanical Design of Process Systems, vol. 2, Gulf Pub. Company, Houston Texas, 1986. [5] Soekardi. C. April 2001. Prediksi karakteristik termal sebuah penukar kalor dampak pemilihan faktor pengotoran konstan, Poros, 4 No 2, 141-150. [6] Soekardi.C. April 2002. Implikasi Perancangan Sebuah penukar kalor dengan faktor Pengotoran dan fungsi waktu terhadap kinerjanya pada kondisi operasi beban thermal konstan, Poros, Vol. 5. NO. p. 129-137. [7] Thurmarimurungan M. 2006. Performance Analysis of Shell and TubeHeat Exchanger Using Miscedle System. American Journal of Applied Sciences. [8] Yulianto S. 2010. Analisa Perancangan Alat Pendingin Jenis Shell And Tube Dengan Cleaning Interval yang Bervariasi. Tesis Program Studi Teknik Mesin Universitas Pancasila.en_US
dc.identifier.issn2407-4330
dc.identifier.urihttp://hdl.handle.net/11617/4955
dc.description.abstractHeat exchangers have been commonly used in industrial processes such as thermal power plant, chemical process, air conditioner device, refrigerator, even in some bigger energy processes like oil and gas. The performance of a heat exchanger is not permanently the same during daily and even annually uses whereas one of the most common causes is the fouling factor. In this research, the performance of a laboratory scale heat exchanger was observed by the inlet and outlet temperature of hot oil and cold water fluids based on characteristic of fouling factor. The flow rates were kept constant at 0.72 m 3 /hour for shell and 0.468 m 3 /hour for tube. The observation time was at 06.00 am, 12.00 am, 18.00 pm, 24.00 pm every day for six respective days. The result shows that ΔT changes irregularly during the observation while the fouling factor increases regularly and decreases significantly by the end of the observation.en_US
dc.publisherUniversitas Muhammadiyah Surakartaen_US
dc.subjectHeat exchangeren_US
dc.subjectfouling factoren_US
dc.subjectshell and tubeen_US
dc.subjectcharacteristicen_US
dc.titleA Study on the Characteristic of Fouling Factor of a Laboratory Scale Shell and Tube Heat Exchangeren_US
dc.typeArticleen_US


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