A design algorithm for batch stirred tank transesterification reactors
► Simplified algorithm for batch biodiesel reactor design was developed. ► C Sharp software tool for implementing the algorithm was also developed. ► 50L/batch reactor was constructed and used to process neem oil biodiesel. ► Results showed that the produced neem biodiesel is a fuel grade product. ►...
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          | Published in | Energy conversion and management Vol. 62; pp. 40 - 46 | 
|---|---|
| Main Authors | , , , , | 
| Format | Journal Article | 
| Language | English | 
| Published | 
        Kidlington
          Elsevier Ltd
    
        01.10.2012
     Elsevier  | 
| Subjects | |
| Online Access | Get full text | 
| ISSN | 0196-8904 1879-2227  | 
| DOI | 10.1016/j.enconman.2012.03.027 | 
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| Abstract | ► Simplified algorithm for batch biodiesel reactor design was developed. ► C Sharp software tool for implementing the algorithm was also developed. ► 50L/batch reactor was constructed and used to process neem oil biodiesel. ► Results showed that the produced neem biodiesel is a fuel grade product. ► Scale-up of the reactor was carried out using the developed software.
A 50L per batch, stirred tank reactor, suitable for carrying out transesterification of vegetable oils was designed and constructed. The major design assumptions included stainless steel plate thickness of 2mm, reaction temperature of 60–65°C and an initial/final fluid temperature of 25/70°C. The calculated impeller Reynolds number was in the mixed regime zone of 10–104; the power number was varied between 1 and 5, while a typical propeller speed of 22.5rev/s (or 1350rev/min) was adopted. The limiting design conditions were maximum reactor diameter of 1.80m, straight side height-to-diameter ratio in the range of 0.75–1.5 and minimum agitator motor power of 746W (1Hp). Based upon the design, a simple algorithm was developed and interpreted into Microsoft C Sharp computer programming language to enable scale up of the reactor. Performance testing of the realized reactor was carried out while using it to produce Neem oil biodiesel via base – catalyzed methanolysis, which yielded high quality fuel product. | 
    
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| AbstractList | ► Simplified algorithm for batch biodiesel reactor design was developed. ► C Sharp software tool for implementing the algorithm was also developed. ► 50L/batch reactor was constructed and used to process neem oil biodiesel. ► Results showed that the produced neem biodiesel is a fuel grade product. ► Scale-up of the reactor was carried out using the developed software.
A 50L per batch, stirred tank reactor, suitable for carrying out transesterification of vegetable oils was designed and constructed. The major design assumptions included stainless steel plate thickness of 2mm, reaction temperature of 60–65°C and an initial/final fluid temperature of 25/70°C. The calculated impeller Reynolds number was in the mixed regime zone of 10–104; the power number was varied between 1 and 5, while a typical propeller speed of 22.5rev/s (or 1350rev/min) was adopted. The limiting design conditions were maximum reactor diameter of 1.80m, straight side height-to-diameter ratio in the range of 0.75–1.5 and minimum agitator motor power of 746W (1Hp). Based upon the design, a simple algorithm was developed and interpreted into Microsoft C Sharp computer programming language to enable scale up of the reactor. Performance testing of the realized reactor was carried out while using it to produce Neem oil biodiesel via base – catalyzed methanolysis, which yielded high quality fuel product. A 50L per batch, stirred tank reactor, suitable for carrying out transesterification of vegetable oils was designed and constructed. The major design assumptions included stainless steel plate thickness of 2mm, reaction temperature of 60–65°C and an initial/final fluid temperature of 25/70°C. The calculated impeller Reynolds number was in the mixed regime zone of 10–10⁴; the power number was varied between 1 and 5, while a typical propeller speed of 22.5rev/s (or 1350rev/min) was adopted. The limiting design conditions were maximum reactor diameter of 1.80m, straight side height-to-diameter ratio in the range of 0.75–1.5 and minimum agitator motor power of 746W (1Hp). Based upon the design, a simple algorithm was developed and interpreted into Microsoft C Sharp computer programming language to enable scale up of the reactor. Performance testing of the realized reactor was carried out while using it to produce Neem oil biodiesel via base – catalyzed methanolysis, which yielded high quality fuel product. A 50 L per batch, stirred tank reactor, suitable for carrying out transesterification of vegetable oils was designed and constructed. The major design assumptions included stainless steel plate thickness of 2 mm, reaction temperature of 60-65 degree C and an initial/final fluid temperature of 25/70 degree C. The calculated impeller Reynolds number was in the mixed regime zone of 10x10 super(4); the power number was varied between 1 and 5, while a typical propeller speed of 22.5 rev/s (or 1350 rev/min) was adopted. The limiting design conditions were maximum reactor diameter of 1.80 m, straight side height-to-diameter ratio in the range of 0.75-1.5 and minimum agitator motor power of 746 W (1 Hp). Based upon the design, a simple algorithm was developed and interpreted into Microsoft C Sharp computer programming language to enable scale up of the reactor. Performance testing of the realized reactor was carried out while using it to produce Neem oil biodiesel via base a catalyzed methanolysis, which yielded high quality fuel product.  | 
    
| Author | Oparaku, O.U. Mbajiorgu, C.C. Anyanwu, C.N. Odigboh, E.U. Emmanuel, U.N.  | 
    
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| Cites_doi | 10.1016/j.enconman.2011.05.008 10.1016/j.renene.2008.04.006 10.13031/2013.7010 10.1007/BF02679605 10.1007/s12155-008-9008-8 10.1016/j.enconman.2010.01.017 10.1016/j.biombioe.2004.02.004 10.2172/15008800 10.5897/AJB11.961 10.1007/s11746-997-0254-2 10.1016/j.enconman.2009.06.021 10.1016/j.enconman.2007.06.016 10.1002/er.1784 10.1016/j.enconman.2008.09.001 10.1016/j.enconman.2005.11.019 10.1590/S0103-50531998000300002 10.1016/j.enconman.2010.12.004 10.1016/j.enconman.2010.10.011  | 
    
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| Keywords | Design CI engine Vegetable oil Reactor Computer software Biodiesel Cl engine  | 
    
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| Snippet | ► Simplified algorithm for batch biodiesel reactor design was developed. ► C Sharp software tool for implementing the algorithm was also developed. ► 50L/batch... A 50 L per batch, stirred tank reactor, suitable for carrying out transesterification of vegetable oils was designed and constructed. The major design... A 50L per batch, stirred tank reactor, suitable for carrying out transesterification of vegetable oils was designed and constructed. The major design...  | 
    
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| SubjectTerms | Agitators Algorithms Applied sciences Biodiesel CI engine Computational fluid dynamics Computer software Design Energy Exact sciences and technology Fluid flow methanolysis neem oil Propellers Reactor Reactors Reynolds number stainless steel Tanks temperature Transesterification Vegetable oil  | 
    
| Title | A design algorithm for batch stirred tank transesterification reactors | 
    
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