2004
DOI: 10.1016/j.energy.2004.03.020
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Rice straw as a bio-oil source via pyrolysis and steam pyrolysis

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Cited by 190 publications
(63 citation statements)
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“…2-a, b, c, d) that are readily adsorbed on soil particles, which reveals the higher DOC-extraction capacity of K 2 SO 4 over H 2 O. The hydrophobic fractions in the K 2 SO 4 extracts are composed of aliphatic constituents rather than aromatic compounds (Table 3), which may be related to the rich aliphatic content of the organic materials in farmland soils, such as straw and cellulose (Putun et al, 2004;Wu, 2013).…”
Section: Discussionmentioning
confidence: 99%
“…2-a, b, c, d) that are readily adsorbed on soil particles, which reveals the higher DOC-extraction capacity of K 2 SO 4 over H 2 O. The hydrophobic fractions in the K 2 SO 4 extracts are composed of aliphatic constituents rather than aromatic compounds (Table 3), which may be related to the rich aliphatic content of the organic materials in farmland soils, such as straw and cellulose (Putun et al, 2004;Wu, 2013).…”
Section: Discussionmentioning
confidence: 99%
“…Hasil ikutan tanaman padi adalah jerami, dedak dan sekam, setiap ton gabah yang dipanen menyisakan jerami padi sekitar 1,35 ton/tahun (Putun et al, 2004), penggilingan gabah yang telah dikeringkan akan dihasilkan sekitar 10% dedak, 2% menir (beras yang rusak/hancur), dan 24-25% sekam. Pemberian jerami padi secara langsung bukanlah pakan yang berkualitas baik karena mengandung kadar protein yang rendah dan serat kasar yang tinggi.…”
Section: Pendahuluanunclassified
“…A quite number of the previous research groups worked for the potential recovery of fuels and chemicals from different agricultural residues and by-products including rice straw [5][6][18][19][20][21], guayule bagasse [7], sesame stalk [11], hazelnut shells [12], olive husk, corncob and tea waste [15], rice husks [22][23][24][25][26], jute stick [27][28], sugarcane bagasse [4,10,17,23,[29][30], olive bagasse [31], sweet sorghum bagasse [32], cotton stalk [33] via pyrolysis in relation to process conditions. Most of the works have been performed for the effect of reactor temperature on the product yields and product compositions but there have been very limited studies for the effect of feed size and vapor residence time.…”
Section: Extractionmentioning
confidence: 99%
“…The reactor bed temperature was varied between 400°C to 500°C at an interval of 25°C while the fluidizing gas flow rate was varied between 22 to 38 l/min at an interval of 4 l/min. To enhance the liquid yields as well as its quality from fast pyrolysis of biomass, several research groups worked with different heating rates including 5°C/min [21], 7°C/min [12], 10°C/min [31], 100-500°C/min [23], 500°C/min [11] and even of 1000°C/sec [17]. However, the presented experiment has been carried out with a heating rate of 100±5°C/min.…”
mentioning
confidence: 99%