1997
DOI: 10.1016/s0016-2361(97)00120-8
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Liquefaction of micro-algae with iron catalyst

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Cited by 110 publications
(64 citation statements)
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“…8 Effect of catalyst level on product distribution in liquefaction of Spirulina in 1-methylnaphthalene under hydrogen at 350 uC for 60 min. 90 with an oil yield of 61 wt% at 350 uC as shown in A preliminary regenerability study indicated that no significant activity loss occurred for regenerated catalysts. Possible pathways for the deoxygenation of stearic acid over heterogeneous catalysts at supercritical water conditions was investigated.…”
Section: Heterogeneous Hydrothermal Liquefaction Of Algae Feedstockmentioning
confidence: 83%
See 1 more Smart Citation
“…8 Effect of catalyst level on product distribution in liquefaction of Spirulina in 1-methylnaphthalene under hydrogen at 350 uC for 60 min. 90 with an oil yield of 61 wt% at 350 uC as shown in A preliminary regenerability study indicated that no significant activity loss occurred for regenerated catalysts. Possible pathways for the deoxygenation of stearic acid over heterogeneous catalysts at supercritical water conditions was investigated.…”
Section: Heterogeneous Hydrothermal Liquefaction Of Algae Feedstockmentioning
confidence: 83%
“…However, bio-oil physico-chemical characteristics, including heating values and distribution of components, were highly influenced by conversion method and feedstock. 89,90,93,142 The use of heterogeneous catalysts during HTL of microalgae was recently reported to produce higher quality bio-oil by lowering the oxygen content in products. Early in 1997, Matsui et al 90 investigated the liquefaction of micro-algae (spirulina) with an iron catalyst (Fe(CO) 5 -S) and obtained 66.9 wt% oil yield at 350 uC for 60 min in tetralin.…”
Section: Heterogeneous Hydrothermal Liquefaction Of Algae Feedstockmentioning
confidence: 99%
“…Liquefaction in water gave an oil yield as high as 78.3 wt % at 350 ° C even under nitrogen without a catalyst. Liquefaction in toluene gave oil fractions having a heating value of 32 -33 MJ/kg, but products obtained in water, containing large amounts of oxygen, were estimated to have a lower heating value of 26 MJ/kg (Matsui et al 1997 ).…”
Section: Conversion Of Algae To Biofuelmentioning
confidence: 97%
“…Matsui et al (1997) investigated the liquefaction of Spirulina , a high -protein microalgae in various organic solvents or water under hydrogen, nitrogen, or carbon monoxide in the temperature range 300 -425 ° C, using Fe(CO)5 -S catalyst. Among the solvents of tetralin, 1 -methylnaphthalene, toluene, and water, it seemed more favorable for liquefaction of Spirulina to take place in water.…”
Section: Conversion Of Algae To Biofuelmentioning
confidence: 99%
“…*Co-products composition depends on the conversion process used. a [20,[23][24][25][26][27][28], b [11,33,37,[56][57][58][59][60][61][62][63][64][65][66][67], c [11,33,56,59,64], d [27,33,[36][37][38][39][40] Transesterification of Extracted Lipids Figure 2 is a flow chart showing the main processes that are required to produce biodiesel, a form of renewable diesel, from extracted algal lipids, which is the most commonly investigated of the three pathways presented here. After algae are grown in an open pond, photobioreactor, or fermentor (i.e., heterotrophic growth), the algae are harvested from the growth medium.…”
Section: Production Pathwaysmentioning
confidence: 99%