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1 of 52.123 pages  |  10  records  |  more records»
OPTIMASI  PEMURNIAN  ASAP CAIR DENGAN METODA REDISTILASI [Optimation of Liquid Smoke Purification by Redistilation Method)   Purnama Darmadji 1) 1) Teknologi Pangan dan Hasil Pertanian, Fakultas Teknologi Pertanian- Universitas Gadjah Mada ... see more
< | p class="MsoNormal" style="text-align:center | " align="center"> | < | strong> | < | span lang="en-gb" xml:lang="en-gb"> | OPTIMASI< | span> |   |  < | /span> | PEMURNIAN< | span> |   |  < | /span> | ASAP CAIR< | /span> | < | /strong> | < | strong> | < | /strong> | < | /p> |  < | h1 style="text-align:center | "> | < | span style="font-size:12pt | " lang="en-gb" xml:lang="en-gb"> | DENGAN METODA REDISTILASI< | /span> | < | /h1> |  < | p class="MsoBodyText3" style="margin-top:12pt | "> | < | span lang="en-gb" xml:lang="en-gb"> | [Optimation of Liquid Smoke Purification by Redistilation Method)< | /span> | < | /p> |  < | p class="MsoNormal" style="text-align:center | " align="center"> | < | span lang="en-gb" xml:lang="en-gb"> |   | < | /span> | < | /p> |  < | h5> | < | span lang="en-gb" xml:lang="en-gb"> | Purnama Darmadji < | sup> | 1)< | /sup> | < | /span> | < | /h5> |  < | p class="MsoNormal" style="margin-top:6pt | text-align:center | " align="center"> | < | sup> | < | span style="font-size:9pt | " lang="en-gb" xml:lang="en-gb"> | 1)< | /span> | < | /sup> | < | span style="font-size:9pt | " lang="en-gb" xml:lang="en-gb"> |  Teknologi Pangan dan Hasil Pertanian |  Fakultas Teknologi Pertanian- Universitas Gadjah Mada< | /span> | < | /p> |  < | p class="MsoNormal" style="text-align:center | " align="center"> | < | span lang="en-gb" xml:lang="en-gb"> |   | < | /span> | < | /p> |  < | p class="MsoNormal" style="text-align:center | " align="center"> | < | strong> | < | span style="font-size:11pt | " lang="en-gb" xml:lang="en-gb"> |   | < | /span> | < | /strong> | < | /p> |  < | p class="MsoHeading8"> | < | span lang="en-gb" xml:lang="en-gb"> | ABSTRACT< | /span> | < | /p> |  < | p class="MsoNormal" style="text-align:center | " align="center"> | < | span lang="en-gb" xml:lang="en-gb"> |   | < | /span> | < | /p> |  < | p class="MsoBodyText"> | < | span style="font-size:9pt | " lang="en-gb" xml:lang="en-gb"> | < | span> |   |   |   |  < | /span> | < | em> | Purification of liquid smoke is very important for< | span> |   |  < | /span> | the safety of the liquid smoke |  because< | span> |   |  < | /span> | of< | span> |   |  < | /span> | content of tar and some carsinogenic substances.< | span> |   |  < | /span> | This research was done using re-distillation process |  with three factor< | span> |   |  < | /span> | treatment including :< | span> |   |  < | /span> | 1) distillation temperature |  distillation time and condensation temperature. The range of distillation temperature was ‹< | span> |   |  < | /span> | 100< | /em> | < | /span> | < | em> | < | span style="font-size:9pt | font-family:Symbol | " lang="en-gb" xml:lang="en-gb"> | < | span> | °< | /span> | < | /span> | < | /em> | < | em> | < | span style="font-size:9pt | " lang="en-gb" xml:lang="en-gb"> | C |  100-125< | /span> | < | /em> | < | em> | < | span style="font-size:9pt | font-family:Symbol | " lang="en-gb" xml:lang="en-gb"> | < | span> | °< | /span> | < | /span> | < | /em> | < | em> | < | span style="font-size:9pt | " lang="en-gb" xml:lang="en-gb"> | C |  125-150< | /span> | < | /em> | < | em> | < | span style="font-size:9pt | font-family:Symbol | " lang="en-gb" xml:lang="en-gb"> | < | span> | °< | /span> | < | /span> | < | /em> | < | em> | < | span style="font-size:9pt | " lang="en-gb" xml:lang="en-gb"> | C< | span> |   |  < | /span> | and< | span> |   |  < | /span> | ›150< | /span> | < | /em> | < | em> | < | span style="font-size:9pt | font-family:Symbol | " lang="en-gb" xml:lang="en-gb"> | < | span> | °< | /span> | < | /span> | < | /em> | < | em> | < | span style="font-size:9pt | " lang="en-gb" xml:lang="en-gb"> | C.< | span> |   |  < | /span> | Distillation time was 30 |  60 and 90 minutes | < | span> |   |  < | /span> | and condensation temperature was : 10-15< | /span> | < | /em> | < | em> | < | span style="font-size:9pt | font-family:Symbol | " lang="en-gb" xml:lang="en-gb"> | < | span> | °< | /span> | < | /span> | < | /em> | < | em> | < | span style="font-size:9pt | " lang="en-gb" xml:lang="en-gb"> | C | < | span> |   |  < | /span> | 15-25< | /span> | < | /em> | < | em> | < | span style="font-size:9pt | font-family:Symbol | " lang="en-gb" xml:lang="en-gb"> | < | span> | °< | /span> | < | /span> | < | /em> | < | em> | < | span style="font-size:9pt | " lang="en-gb" xml:lang="en-gb"> | C and 25-30< | /span> | < | /em> | < | em> | < | span style="font-size:9pt | font-family:Symbol | " lang="en-gb" xml:lang="en-gb"> | < | span> | °< | /span> | < | /span> | < | /em> | < | em> | < | span style="font-size:9pt | " lang="en-gb" xml:lang="en-gb"> | C. The results indicated no detected tar content in the purified liquid smoke |  and optimum condition for redistillation process was< | span> |   |   |  < | /span> | : 122.5< | /span> | < | /em> | < | em> | < | span style="font-size:9pt | font-family:Symbol | " lang="en-gb" xml:lang="en-gb"> | < | span> | °< | /span> | < | /span> | < | /em> | < | em> | < | span style="font-size:9pt | " lang="en-gb" xml:lang="en-gb"> | C< | span> |   |  < | /span> | for distillation temperature |  distillation time was< | span> |   |  < | /span> | 69 minutes and condensation temperature was< | span> |   |  < | /span> | 24< | /span> | < | /em> | < | em> | < | span style="font-size:9pt | font-family:Symbol | " lang="en-gb" xml:lang="en-gb"> | < | span> | °< | /span> | < | /span> | < | /em> | < | em> | < | span style="font-size:9pt | " lang="en-gb" xml:lang="en-gb"> | C. At this optimum condition the value of< | span> |   |  < | /span> | phenol |  carbonyl and total acid were 2.24% |  5.60% and 15.7% |  respectively. < | /span> | < | /em> | < | /p> |  < | p class="MsoBodyText"> | < | span lang="en-gb" xml:lang="en-gb"> |   | < | /span> | < | /p> |  < | p class="MsoBodyText" style="text-indent:0cm | "> | < | strong> | < | span style="font-size:9pt | " lang="en-gb" xml:lang="en-gb"> | Key words< | /span> | < | /strong> | < | span style="font-size:9pt | " lang="en-gb" xml:lang="en-gb"> | : < | em> | Liquid smoke |  redistilation and optimum condition of redistilation.< | span> |   |  < | /span> | < | /em> | < | /span> | < | em> | < | /em> | < | /p> |  < | p class="MsoNormal" style="text-align:center | " align="center"> | < | strong> | < | span style="font-size:11pt | " lang="en-gb" xml:lang="en-gb"> |   | < | /span> | < | /strong> | < | /p> | 
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The rapid development of Crude Palm Oil (CPO) production has led to an increase in the production of Palm Oil Mill Effluent (POME) as well. POME will cause problems in the environment because contains high contaminants. This study aims to investigate the ... see more

Hospital wastewater basically contains organic materials and inorganic materials. Levels of these materials can be determined by testing of Biochemical Oxygen Demand (BOD), Chemical Oxygen Demand (COD), Total Dissolved Solid (TDS), and Total Suspended Sol... see more

The highest percentage in home electricity demands in Brazil lies with the water heating systems, where the electric shower has a great contribution in consumption. The use of solar thermal panels is an alternative to minimize the strain on the electrical... see more

Liquid waste is easily recognized because of the presence of dyes. Waste containing dyes can cause visual pollution and increase the risk of environmental and health damage. The aim of this study was to determine the operating conditions of the best jumpu... see more

The rapid development of Crude Palm Oil (CPO) production has led to an increase in the production of Palm Oil Mill Effluent (POME) as well. POME will cause problems in the environment because contains high contaminants. This study aims to investigate the ... see more

1 of 52.123 pages  |  10  records  |  more records»