1991
DOI: 10.2172/5086913
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Research on the pyrolysis of hardwood in an entrained bed process development unit

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Cited by 7 publications
(3 citation statements)
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“…At pyrolysis temperature of about 500°C, a maximum yield of about 50% liquid and 30% gas is expected. The holding carbonization time is usually calculated based on the reactor height and the gas flow rates but usually made of several seconds [48]. One major problem of this technique is the low heat produced by the entraining gas which usually leads to low liquid yield since biomass requires high heat for a high liquid yield.…”
Section: Georgia Tech Entrained Bed Processmentioning
confidence: 99%
“…At pyrolysis temperature of about 500°C, a maximum yield of about 50% liquid and 30% gas is expected. The holding carbonization time is usually calculated based on the reactor height and the gas flow rates but usually made of several seconds [48]. One major problem of this technique is the low heat produced by the entraining gas which usually leads to low liquid yield since biomass requires high heat for a high liquid yield.…”
Section: Georgia Tech Entrained Bed Processmentioning
confidence: 99%
“…3) developed in the late 1970's to the early 1980's, Kovac et al [18]. Here the biomass feed is crushed to Illustration of the Garrett process [17].…”
Section: Georgia Tech Entrained Bed Processmentioning
confidence: 99%
“…The reactor was a bottom fed with roughly 1.5 ton/day hardwood biomass and achieved bio-oil yields up to 60 wt % on a dry basis. Georgia Tech Research Institute operated the reactor from 1982 until 1989 [51]. Even though entrained flow reactors may be fed from the bottom which requires large amounts of carrier gas to entrain the feedstock, the reactor shares a tubular shape and may be heated in a similar fashion as a free-fall reactor [43].…”
Section: Figure 3 Ablative Reactor Types A) Spinning Disk and B) Vormentioning
confidence: 99%