首页> 外文期刊>International journal of hydrogen energy >Feasibility of bio-hythane production by co-digesting skim latex serum (SLS) with palm oil mill effluent (POME) through two-phase anaerobic process
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Feasibility of bio-hythane production by co-digesting skim latex serum (SLS) with palm oil mill effluent (POME) through two-phase anaerobic process

机译:通过两相厌氧工艺共同消化脱脂乳胶血清(SLS)与棕榈油厂废液(POME)来生产生物丙烷的可行性

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Hydrogenogenic batch fermentation without nutrients addition was investigated at different SLS: POME mixing ratios of 100:0, 95:5, 90:10, 85:15, 80:20, 75:25, 70:30, 65:35, 60:40, 55:45,50:50, and 0:100 (Volatile Solid, VS basis) at initial organic concentrations of 21 and 7 g-VS/L. Satisfactory hydrogen yield of 84.5 +/- 0.7 mL H(2)g-VSadded was achieved from 7 gVS/L batch having SLS: POME-VS mixing ratio of 55:45. Adding NaHCO3 3 g/L or 0.43 gNaHCCO(3)/g-VS) in the two-stage anaerobic system at 7 g-VS/L could provide sufficient buffering capacity. Hydrogenogenic effluent from 7 g-VS/L batch at SLS: POME mixing ratio of 55:45 (VS basis) could further generate rather high methane yield of 311.2 +/- 8.0 mL- CH4/ g-VSadded in themethanogenic stage.According to the experimental results, bio-hythane approximately 55.5 x 10(6) m(3)/year with 21% (V/V) of hydrogen, equivalent to51.0 x 10(6) lgasoline could be produced potentially from 3.88 x 10(6) m(3) of mixed SLS and POME through the two-stage anaerobic co-digestion. (C) 2018 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:在不同的SLS:POME混合比为100:0、95:5、90:10、85:15、80:20、75:25、70:30、65:35、60: 40、55:45、50:50和0:100(挥发性固体,以VS为基准),初始有机浓度为21和7 g-VS / L。从SLS:POME-VS混合比为55:45的7 gVS / L批料中获得令人满意的氢产量84.5 +/- 0.7 mL H(2)g-VS。在两级厌氧系统中以7 g-VS / L添加3 g / L的NaHCO3或0.43 gNaHCCO(3)/ g-VS)可以提供足够的缓冲能力。在SLS:POME混合比为55:45(以VS为基准)下,来自7 g-VS / L批次的制氢废水可进一步产生相当高的甲烷产率,甲烷生成阶段添加的甲烷产量为311.2 +/- 8.0 mL-CH4 / g-VS。实验结果显示,每年可从3.88 x 10(约55.5 x 10(6)m(3)/氢,相当于51.0 x 10(6)汽油生成生物bio烷。 6)m(3)通过两阶段厌氧共消化混合SLS和POME。 (C)2018氢能出版物有限公司。由Elsevier Ltd.出版。保留所有权利。

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