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首页> 外文期刊>Journal of Chemical Engineering of Japan >A Proposal for Zero Emission from Palm Oil Industry Incorporating the Production of Polyhydroxyalkanoates from Palm Oil Mill Effluent
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A Proposal for Zero Emission from Palm Oil Industry Incorporating the Production of Polyhydroxyalkanoates from Palm Oil Mill Effluent

机译:关于将棕榈油厂废水中的聚羟基链烷酸酯生产纳入其中的棕榈油工业零排放的提案

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References(15) Cited-By(16) In our previous reports, we have described the production of organic acids from palm oil mill effluent (POME) which were used as fermentation substrates to produce polyhydroxyalkanoates (PHA). Here we propose a zero emission from palm oil industry incorporating the production of PHA from POME. Our results showed that by evaporation, the organic acids could be concentrated to about 100 g·l–1 for use as substrates for the fed-batch PHA fermentation. Upon condensation of the steam, the water had a COD of 80 ppm, low enough for it to be either recycled or discharged. It was confirmed that the energy for the evaporation can be provided by combusting solid wastes such as shells and empty oil palm bunches. The concentrated organic acids were successfully converted to PHA by Ralstonia eutropha strain ATCC 17699 under a non-sterile fermentation system when the initial cell density was kept high at 4 g·l–1. After 150 hours, 20 g·l–1 cells were obtained with more than 50% PHA content. A repeated fed-batch system was also performed to obtain a high cell inoculum and to mimic the operation of a large PHA production fermentor at C/N ratios of 15 and 30 respectively, with only acetic and propionic acids as carbon sources. It was suggested that the energy for this proposed process could be sufficiently supplied by combustion of the solid wastes from the palm oil mill.
机译:参考文献(15)Cited-By(16)在我们以前的报告中,我们描述了棕榈油厂废液(POME)中有机酸的生产,这些有机酸被用作发酵底物以生产聚羟基链烷酸酯(PHA)。在这里,我们提出了棕榈油工业的零排放,并结合了POME生产的PHA。我们的结果表明,通过蒸发,有机酸可浓缩至约100 g·l–1,用作分批补料PHA发酵的底物。蒸汽冷凝后,水的COD为80 ppm,足够低以至于可以再循环或排放。可以确认,蒸发能量可以通过燃烧固体废物(例如贝壳和空的油棕串)来提供。当初始细胞密度保持在4 g·l–1的高浓度时,富集的有机酸在非无菌发酵系统下被富营养的Ralstonia eutropha菌株ATCC 17699成功转化为PHA。 150小时后,获得20 g·l-1个细胞的PHA含量超过50%。还进行了重复的分批补料系统,以获得高细胞接种量,并模拟分别以C / N为15和30的大型PHA生产发酵罐的运行,仅使用乙酸和丙酸作为碳源。有人提出,通过燃烧棕榈油厂的固体废物,可以为这种拟议方法提供足够的能量。

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