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 inEnergy conversion and management Vol. 62; pp. 40 - 46
Main Authors Anyanwu, C.N., Mbajiorgu, C.C., Oparaku, O.U., Odigboh, E.U., Emmanuel, U.N.
Format Journal Article
LanguageEnglish
Published Kidlington Elsevier Ltd 01.10.2012
Elsevier
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Online AccessGet full text
ISSN0196-8904
1879-2227
DOI10.1016/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.
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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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
URI https://dx.doi.org/10.1016/j.enconman.2012.03.027
https://www.proquest.com/docview/1365115091
https://www.proquest.com/docview/1710214989
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