This paper is concerned with performing laboratory scale alkali-catalyst transesterification for biodiesel reaction and ranking conversion and performance between a stirred tank reactor, and oscillatory flow meso reactors in both batch and continuous mode. The results show that a comparative conversion can be achieved for the same reaction conditions, thereby demonstrating that batch and continuous meso reactor configurations can be used for a high throughput screening biodiesel reactions.
机构:
Chonbuk Natl Univ, Dept Mech Engn, Res Ctr Ind Technol, Jeonju 561756, South KoreaChonbuk Natl Univ, Dept Mech Engn, Res Ctr Ind Technol, Jeonju 561756, South Korea
Choi, Seung-Hun
Oh, Younhtaig
论文数: 0引用数: 0
h-index: 0
机构:
Chonbuk Natl Univ, Dept Mech Engn, Res Ctr Ind Technol, Jeonju 561756, South KoreaChonbuk Natl Univ, Dept Mech Engn, Res Ctr Ind Technol, Jeonju 561756, South Korea
Oh, Younhtaig
[J].
INTERNATIONAL JOURNAL OF MODERN PHYSICS B,
2006,
20
(25-27):
: 4481
-
4486
机构:
Chonbuk Natl Univ, Dept Mech Engn, Res Ctr Ind Technol, Jeonju 561756, South KoreaChonbuk Natl Univ, Dept Mech Engn, Res Ctr Ind Technol, Jeonju 561756, South Korea
Choi, Seung-Hun
Oh, Younhtaig
论文数: 0引用数: 0
h-index: 0
机构:
Chonbuk Natl Univ, Dept Mech Engn, Res Ctr Ind Technol, Jeonju 561756, South KoreaChonbuk Natl Univ, Dept Mech Engn, Res Ctr Ind Technol, Jeonju 561756, South Korea
Oh, Younhtaig
[J].
INTERNATIONAL JOURNAL OF MODERN PHYSICS B,
2006,
20
(25-27):
: 4481
-
4486