Please use this identifier to cite or link to this item: http://repository.ipb.ac.id/handle/123456789/58755
Full metadata record
DC FieldValueLanguage
dc.contributor.advisorPurwanto, Y. Aris
dc.contributor.advisorSunandar, Kudrat
dc.contributor.authorLestari, Nunik
dc.date.accessioned2012-12-07T02:54:23Z
dc.date.available2012-12-07T02:54:23Z
dc.date.issued2012
dc.identifier.urihttp://repository.ipb.ac.id/handle/123456789/58755
dc.description.abstractTamanu (Calophyllum inophyllum L.) has potential as a biofuel producer crop. Tamanu oil has a high viscosity compared with kerosene. Tamanu oil viscosity must be lowered to the equivalent of kerosene to be applied as a substitute for kerosene, especially in pressure stove. In pressure stove, preheating can reduce the viscosity of fuel to achieve the desired viscosity to be sprayed and burned well. Nowadays, pressure stoves generally are made for kerosene fuel. so that, the pressure stove needs to be modified by considering the preheating stage. Thus, the tamanu oil can be used in the modified pressure stove as a subtitute of kerosene. The objective of the study were (1) to simulate the temperature and viscosity change in relation to the length of heating oil pipeline, (2) to modify the heating oil pipeline based on the simulation result, and (3) to test the performance of modified heating oil pipeline. The simulation results show that the oil should be heated to 161.81 °C to obtain the viscosity of tamanu oil close to the viscosity of kerosene, which is using the heating pipe element along the 25 cm. The tamanu oil spraying diameter is 65.67 mm, and the spraying angle is 12.49o. While kerosene as a control has a spraying diameter of 66.75 mm, and the spraying angle is 12.69o. The increasing of spray diameter to temperature follows the equation d = 0.435T + 2.552, with determinant coefficient of 0.961. While the increasing of spray angle to temperature follows the equation θ = 0.082T + 0.51, with determinant coefficient of 0.961. The increase in diameter and angle of spray with increasing oil temperature, due to the increasing temperatures will further lower the viscosity value, surface tension, and density of tamanu oil. According to Ing et al. (2010), viscosity, surface tension, and density are three fluid properties that are influential in forming the droplet. This oil heating element can heat the tamanu oil until 168.5 oC and 164.7 °C for two different data retrieval conditions.en
dc.subjecttamanu oilen
dc.subjectkeroseneen
dc.subjectheatingen
dc.subjectheat transfeen
dc.subjecttemperatureen
dc.subjectviscosityen
dc.subjectsprayingen
dc.subjectdropleten
dc.subjectpressure stoveen
dc.subjectmodificationen
dc.titlePerformance Test of Tamanu Oil for Pressure Stove Modificationen
dc.titleUji Karakteristik Minyak Nyamplung untuk Modifikasi Kompor Bertekanan
Appears in Collections:MT - Agriculture Technology

Files in This Item:
File Description SizeFormat 
2012nle.pdf
  Restricted Access
Fulltext2.91 MBAdobe PDFView/Open
Abstract.pdf
  Restricted Access
Abstract457.29 kBAdobe PDFView/Open
BAB I Pendahuluan.pdf
  Restricted Access
BAB I382.27 kBAdobe PDFView/Open
BAB II Tinjauan Pustaka.pdf
  Restricted Access
BAB II1.03 MBAdobe PDFView/Open
BAB III Metodooi Penelitian.pdf
  Restricted Access
BAB III660.36 kBAdobe PDFView/Open
BAB IV Hasil dan Pembahasan.pdf
  Restricted Access
BAB IV1.41 MBAdobe PDFView/Open
BAB V Kesimpulan dan Saran.pdf
  Restricted Access
BAB V367.26 kBAdobe PDFView/Open
Cover.pdf
  Restricted Access
Cover290.6 kBAdobe PDFView/Open
Daftar Pustaka.pdf
  Restricted Access
Daftar Pustaka438 kBAdobe PDFView/Open
Lampriran.pdf
  Restricted Access
Lampiran1.25 MBAdobe PDFView/Open


Items in DSpace are protected by copyright, with all rights reserved, unless otherwise indicated.