The Experts below are selected from a list of 267 Experts worldwide ranked by ideXlab platform
Dewi Handayani - One of the best experts on this subject based on the ideXlab platform.
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KONVERSI KONVERSI BIOGASOLIN DARI RESIDU MINYAK PALM OIL MILLS EFFLUENT (POME) DENGAN BANTUAN IRADIASI ULTRASONIK DAN PERENGKAHAN KATALITIK
'Asosiasi Agroindustri Indonesia (AGRIN)', 2018Co-Authors: Dewi Handayani, Agus Sundaryono, Arsela Eko Listiono, Lutfi M. FirdausAbstract:Palm oil mill effluent (POME) is a liquid waste by product of fresh fruit bunches processing (FFB) in palm oil factory (POF). POME contains oil residue of 0.7% (from treated FFB). The purpose of this study was to convert oil residue of POME into biogasolin with the help of ultrasonic irradiation and catalytic cracking. The convertion was performed by reacting oil residue of POME with methanol in an esterification and transesterification reaction with the aid of ultrasonic irradiation. The reaction product was further reacted in the catalytic cracking reaction using zeolite-based catalysts (Ni/HZa and Mo-Ni/HZa). The overall reaction results were characterized using GCMS to determine the constituent components. The components found using Mo-Ni/HZa catalyst were 51.22% Biogasoline and other products of kerosene and diesel as well as long chain methyl ester components, whereas using Ni/HZa catalyst was found a component equivalent to diesel at 2.44%.Keywords: Biogasoline, ultrasonic irradiation, catalytic cracking, zeolite catalyst, POM
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konversi konversi biogasolin dari residu minyak palm oil mills effluent pome dengan bantuan iradiasi ultrasonik dan perengkahan katalitik
Journal of Agroindustrial Technology, 2018Co-Authors: Agus Sundaryono, Arsela Eko Listiono, Lutfi M. Firdaus, Dewi HandayaniAbstract:Palm oil mill effluent (POME) is a liquid waste by product of fresh fruit bunches processing (FFB) in palm oil factory (POF). POME contains oil residue of 0.7% (from treated FFB). The purpose of this study was to convert oil residue of POME into biogasolin with the help of ultrasonic irradiation and catalytic cracking. The convertion was performed by reacting oil residue of POME with methanol in an esterification and transesterification reaction with the aid of ultrasonic irradiation. The reaction product was further reacted in the catalytic cracking reaction using zeolite-based catalysts (Ni/HZa and Mo-Ni/HZa). The overall reaction results were characterized using GCMS to determine the constituent components. The components found using Mo-Ni/HZa catalyst were 51.22% Biogasoline and other products of kerosene and diesel as well as long chain methyl ester components, whereas using Ni/HZa catalyst was found a component equivalent to diesel at 2.44%. Keywords: Biogasoline, ultrasonic irradiation, catalytic cracking, zeolite catalyst, POME
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KONVERSI KONVERSI BIOGASOLIN DARI RESIDU MINYAK PALM OIL MILLS EFFLUENT (POME) DENGAN BANTUAN IRADIASI ULTRASONIK DAN PERENGKAHAN KATALITIK
Asosiasi Agroindustri Indonesia, 2018Co-Authors: Agus Sundaryono, Arsela Eko Listiono, Lutfi M. Firdaus, Dewi HandayaniAbstract:Palm oil mill effluent (POME) is a liquid waste by product of fresh fruit bunches processing (FFB) in palm oil factory (POF). POME contains oil residue of 0.7% (from treated FFB). The purpose of this study was to convert oil residue of POME into biogasolin with the help of ultrasonic irradiation and catalytic cracking. The convertion was performed by reacting oil residue of POME with methanol in an esterification and transesterification reaction with the aid of ultrasonic irradiation. The reaction product was further reacted in the catalytic cracking reaction using zeolite-based catalysts (Ni/HZa and Mo-Ni/HZa). The overall reaction results were characterized using GCMS to determine the constituent components. The components found using Mo-Ni/HZa catalyst were 51.22% Biogasoline and other products of kerosene and diesel as well as long chain methyl ester components, whereas using Ni/HZa catalyst was found a component equivalent to diesel at 2.44%
Lutfi M. Firdaus - One of the best experts on this subject based on the ideXlab platform.
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KONVERSI KONVERSI BIOGASOLIN DARI RESIDU MINYAK PALM OIL MILLS EFFLUENT (POME) DENGAN BANTUAN IRADIASI ULTRASONIK DAN PERENGKAHAN KATALITIK
'Asosiasi Agroindustri Indonesia (AGRIN)', 2018Co-Authors: Dewi Handayani, Agus Sundaryono, Arsela Eko Listiono, Lutfi M. FirdausAbstract:Palm oil mill effluent (POME) is a liquid waste by product of fresh fruit bunches processing (FFB) in palm oil factory (POF). POME contains oil residue of 0.7% (from treated FFB). The purpose of this study was to convert oil residue of POME into biogasolin with the help of ultrasonic irradiation and catalytic cracking. The convertion was performed by reacting oil residue of POME with methanol in an esterification and transesterification reaction with the aid of ultrasonic irradiation. The reaction product was further reacted in the catalytic cracking reaction using zeolite-based catalysts (Ni/HZa and Mo-Ni/HZa). The overall reaction results were characterized using GCMS to determine the constituent components. The components found using Mo-Ni/HZa catalyst were 51.22% Biogasoline and other products of kerosene and diesel as well as long chain methyl ester components, whereas using Ni/HZa catalyst was found a component equivalent to diesel at 2.44%.Keywords: Biogasoline, ultrasonic irradiation, catalytic cracking, zeolite catalyst, POM
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konversi konversi biogasolin dari residu minyak palm oil mills effluent pome dengan bantuan iradiasi ultrasonik dan perengkahan katalitik
Journal of Agroindustrial Technology, 2018Co-Authors: Agus Sundaryono, Arsela Eko Listiono, Lutfi M. Firdaus, Dewi HandayaniAbstract:Palm oil mill effluent (POME) is a liquid waste by product of fresh fruit bunches processing (FFB) in palm oil factory (POF). POME contains oil residue of 0.7% (from treated FFB). The purpose of this study was to convert oil residue of POME into biogasolin with the help of ultrasonic irradiation and catalytic cracking. The convertion was performed by reacting oil residue of POME with methanol in an esterification and transesterification reaction with the aid of ultrasonic irradiation. The reaction product was further reacted in the catalytic cracking reaction using zeolite-based catalysts (Ni/HZa and Mo-Ni/HZa). The overall reaction results were characterized using GCMS to determine the constituent components. The components found using Mo-Ni/HZa catalyst were 51.22% Biogasoline and other products of kerosene and diesel as well as long chain methyl ester components, whereas using Ni/HZa catalyst was found a component equivalent to diesel at 2.44%. Keywords: Biogasoline, ultrasonic irradiation, catalytic cracking, zeolite catalyst, POME
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KONVERSI KONVERSI BIOGASOLIN DARI RESIDU MINYAK PALM OIL MILLS EFFLUENT (POME) DENGAN BANTUAN IRADIASI ULTRASONIK DAN PERENGKAHAN KATALITIK
Asosiasi Agroindustri Indonesia, 2018Co-Authors: Agus Sundaryono, Arsela Eko Listiono, Lutfi M. Firdaus, Dewi HandayaniAbstract:Palm oil mill effluent (POME) is a liquid waste by product of fresh fruit bunches processing (FFB) in palm oil factory (POF). POME contains oil residue of 0.7% (from treated FFB). The purpose of this study was to convert oil residue of POME into biogasolin with the help of ultrasonic irradiation and catalytic cracking. The convertion was performed by reacting oil residue of POME with methanol in an esterification and transesterification reaction with the aid of ultrasonic irradiation. The reaction product was further reacted in the catalytic cracking reaction using zeolite-based catalysts (Ni/HZa and Mo-Ni/HZa). The overall reaction results were characterized using GCMS to determine the constituent components. The components found using Mo-Ni/HZa catalyst were 51.22% Biogasoline and other products of kerosene and diesel as well as long chain methyl ester components, whereas using Ni/HZa catalyst was found a component equivalent to diesel at 2.44%
Agus Sundaryono - One of the best experts on this subject based on the ideXlab platform.
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KONVERSI KONVERSI BIOGASOLIN DARI RESIDU MINYAK PALM OIL MILLS EFFLUENT (POME) DENGAN BANTUAN IRADIASI ULTRASONIK DAN PERENGKAHAN KATALITIK
'Asosiasi Agroindustri Indonesia (AGRIN)', 2018Co-Authors: Dewi Handayani, Agus Sundaryono, Arsela Eko Listiono, Lutfi M. FirdausAbstract:Palm oil mill effluent (POME) is a liquid waste by product of fresh fruit bunches processing (FFB) in palm oil factory (POF). POME contains oil residue of 0.7% (from treated FFB). The purpose of this study was to convert oil residue of POME into biogasolin with the help of ultrasonic irradiation and catalytic cracking. The convertion was performed by reacting oil residue of POME with methanol in an esterification and transesterification reaction with the aid of ultrasonic irradiation. The reaction product was further reacted in the catalytic cracking reaction using zeolite-based catalysts (Ni/HZa and Mo-Ni/HZa). The overall reaction results were characterized using GCMS to determine the constituent components. The components found using Mo-Ni/HZa catalyst were 51.22% Biogasoline and other products of kerosene and diesel as well as long chain methyl ester components, whereas using Ni/HZa catalyst was found a component equivalent to diesel at 2.44%.Keywords: Biogasoline, ultrasonic irradiation, catalytic cracking, zeolite catalyst, POM
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konversi konversi biogasolin dari residu minyak palm oil mills effluent pome dengan bantuan iradiasi ultrasonik dan perengkahan katalitik
Journal of Agroindustrial Technology, 2018Co-Authors: Agus Sundaryono, Arsela Eko Listiono, Lutfi M. Firdaus, Dewi HandayaniAbstract:Palm oil mill effluent (POME) is a liquid waste by product of fresh fruit bunches processing (FFB) in palm oil factory (POF). POME contains oil residue of 0.7% (from treated FFB). The purpose of this study was to convert oil residue of POME into biogasolin with the help of ultrasonic irradiation and catalytic cracking. The convertion was performed by reacting oil residue of POME with methanol in an esterification and transesterification reaction with the aid of ultrasonic irradiation. The reaction product was further reacted in the catalytic cracking reaction using zeolite-based catalysts (Ni/HZa and Mo-Ni/HZa). The overall reaction results were characterized using GCMS to determine the constituent components. The components found using Mo-Ni/HZa catalyst were 51.22% Biogasoline and other products of kerosene and diesel as well as long chain methyl ester components, whereas using Ni/HZa catalyst was found a component equivalent to diesel at 2.44%. Keywords: Biogasoline, ultrasonic irradiation, catalytic cracking, zeolite catalyst, POME
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KONVERSI KONVERSI BIOGASOLIN DARI RESIDU MINYAK PALM OIL MILLS EFFLUENT (POME) DENGAN BANTUAN IRADIASI ULTRASONIK DAN PERENGKAHAN KATALITIK
Asosiasi Agroindustri Indonesia, 2018Co-Authors: Agus Sundaryono, Arsela Eko Listiono, Lutfi M. Firdaus, Dewi HandayaniAbstract:Palm oil mill effluent (POME) is a liquid waste by product of fresh fruit bunches processing (FFB) in palm oil factory (POF). POME contains oil residue of 0.7% (from treated FFB). The purpose of this study was to convert oil residue of POME into biogasolin with the help of ultrasonic irradiation and catalytic cracking. The convertion was performed by reacting oil residue of POME with methanol in an esterification and transesterification reaction with the aid of ultrasonic irradiation. The reaction product was further reacted in the catalytic cracking reaction using zeolite-based catalysts (Ni/HZa and Mo-Ni/HZa). The overall reaction results were characterized using GCMS to determine the constituent components. The components found using Mo-Ni/HZa catalyst were 51.22% Biogasoline and other products of kerosene and diesel as well as long chain methyl ester components, whereas using Ni/HZa catalyst was found a component equivalent to diesel at 2.44%
Chen Zhao - One of the best experts on this subject based on the ideXlab platform.
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selective deoxygenation of aqueous furfural to 2 methylfuran over cu0 cu2o sio2 sites via a copper phyllosilicate precursor without extraneous gas
ACS Sustainable Chemistry & Engineering, 2018Co-Authors: Hao Sun, Chen ZhaoAbstract:Furfural (FUL) is substantially produced by the polymeric xylan fraction of hemicellulose with the presence of acids, and 2-methyl furan (2-MF) produced from FUL is an important Biogasoline additive. Here, we report that 2-MF can be selectively formed from FUL with a 90% yield at 220 °C within 2 h over Cu0/Cu2O·SiO2 sites via a copper phyllosilicate precursor without extraneous gas. Methanol is used for in situ generating of highly pure hydrogen (92% content), and the almost CO free atmosphere avoids the poison on the Cu sites. The structure–activity relationship shows that Cu0 or Cu2O or physically mixed Cu0 and Cu2O is inactive, but the hydrogen-reduced copper phyllosilicate sample comprising abundant Cu0/Cu2O·SiO2 sites with interfaces demonstrates high activities in both reactions of methanol decomposition and FUL hydrodeoxygenation (HDO). The network for converting FUL to 2-MF includes tandem steps of FUL hydrogenation and furfural alcohol (FOL) hydrogenolysis to target 2-MF, accompanied by the side-...
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Selective Deoxygenation of Aqueous Furfural to 2‑Methylfuran over Cu0/Cu2O·SiO2 Sites via a Copper Phyllosilicate Precursor without Extraneous Gas
2018Co-Authors: Hao Sun, Chen ZhaoAbstract:Furfural (FUL) is substantially produced by the polymeric xylan fraction of hemicellulose with the presence of acids, and 2-methyl furan (2-MF) produced from FUL is an important Biogasoline additive. Here, we report that 2-MF can be selectively formed from FUL with a 90% yield at 220 °C within 2 h over Cu0/Cu2O·SiO2 sites via a copper phyllosilicate precursor without extraneous gas. Methanol is used for in situ generating of highly pure hydrogen (92% content), and the almost CO free atmosphere avoids the poison on the Cu sites. The structure–activity relationship shows that Cu0 or Cu2O or physically mixed Cu0 and Cu2O is inactive, but the hydrogen-reduced copper phyllosilicate sample comprising abundant Cu0/Cu2O·SiO2 sites with interfaces demonstrates high activities in both reactions of methanol decomposition and FUL hydrodeoxygenation (HDO). The network for converting FUL to 2-MF includes tandem steps of FUL hydrogenation and furfural alcohol (FOL) hydrogenolysis to target 2-MF, accompanied by the side-reactions of hydrogenation of furan rings and ring opening of 2-MF. The kinetics modeling shows that the rational manipulation of reaction parameters of temperatures, reaction times, and H2 amounts is the key for attaining high yields of 2-MF. Eventually, the crude aqueous FUL solution with 10 wt % water can be selectivity hydrodeoxygenated to 2-MF (close to 90% yield) at the used catalytic conditions
Arsela Eko Listiono - One of the best experts on this subject based on the ideXlab platform.
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KONVERSI KONVERSI BIOGASOLIN DARI RESIDU MINYAK PALM OIL MILLS EFFLUENT (POME) DENGAN BANTUAN IRADIASI ULTRASONIK DAN PERENGKAHAN KATALITIK
'Asosiasi Agroindustri Indonesia (AGRIN)', 2018Co-Authors: Dewi Handayani, Agus Sundaryono, Arsela Eko Listiono, Lutfi M. FirdausAbstract:Palm oil mill effluent (POME) is a liquid waste by product of fresh fruit bunches processing (FFB) in palm oil factory (POF). POME contains oil residue of 0.7% (from treated FFB). The purpose of this study was to convert oil residue of POME into biogasolin with the help of ultrasonic irradiation and catalytic cracking. The convertion was performed by reacting oil residue of POME with methanol in an esterification and transesterification reaction with the aid of ultrasonic irradiation. The reaction product was further reacted in the catalytic cracking reaction using zeolite-based catalysts (Ni/HZa and Mo-Ni/HZa). The overall reaction results were characterized using GCMS to determine the constituent components. The components found using Mo-Ni/HZa catalyst were 51.22% Biogasoline and other products of kerosene and diesel as well as long chain methyl ester components, whereas using Ni/HZa catalyst was found a component equivalent to diesel at 2.44%.Keywords: Biogasoline, ultrasonic irradiation, catalytic cracking, zeolite catalyst, POM
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konversi konversi biogasolin dari residu minyak palm oil mills effluent pome dengan bantuan iradiasi ultrasonik dan perengkahan katalitik
Journal of Agroindustrial Technology, 2018Co-Authors: Agus Sundaryono, Arsela Eko Listiono, Lutfi M. Firdaus, Dewi HandayaniAbstract:Palm oil mill effluent (POME) is a liquid waste by product of fresh fruit bunches processing (FFB) in palm oil factory (POF). POME contains oil residue of 0.7% (from treated FFB). The purpose of this study was to convert oil residue of POME into biogasolin with the help of ultrasonic irradiation and catalytic cracking. The convertion was performed by reacting oil residue of POME with methanol in an esterification and transesterification reaction with the aid of ultrasonic irradiation. The reaction product was further reacted in the catalytic cracking reaction using zeolite-based catalysts (Ni/HZa and Mo-Ni/HZa). The overall reaction results were characterized using GCMS to determine the constituent components. The components found using Mo-Ni/HZa catalyst were 51.22% Biogasoline and other products of kerosene and diesel as well as long chain methyl ester components, whereas using Ni/HZa catalyst was found a component equivalent to diesel at 2.44%. Keywords: Biogasoline, ultrasonic irradiation, catalytic cracking, zeolite catalyst, POME
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KONVERSI KONVERSI BIOGASOLIN DARI RESIDU MINYAK PALM OIL MILLS EFFLUENT (POME) DENGAN BANTUAN IRADIASI ULTRASONIK DAN PERENGKAHAN KATALITIK
Asosiasi Agroindustri Indonesia, 2018Co-Authors: Agus Sundaryono, Arsela Eko Listiono, Lutfi M. Firdaus, Dewi HandayaniAbstract:Palm oil mill effluent (POME) is a liquid waste by product of fresh fruit bunches processing (FFB) in palm oil factory (POF). POME contains oil residue of 0.7% (from treated FFB). The purpose of this study was to convert oil residue of POME into biogasolin with the help of ultrasonic irradiation and catalytic cracking. The convertion was performed by reacting oil residue of POME with methanol in an esterification and transesterification reaction with the aid of ultrasonic irradiation. The reaction product was further reacted in the catalytic cracking reaction using zeolite-based catalysts (Ni/HZa and Mo-Ni/HZa). The overall reaction results were characterized using GCMS to determine the constituent components. The components found using Mo-Ni/HZa catalyst were 51.22% Biogasoline and other products of kerosene and diesel as well as long chain methyl ester components, whereas using Ni/HZa catalyst was found a component equivalent to diesel at 2.44%