“…27,68,70,115,140−151 Catalytic tar cracking is considered to be promising, as it can be performed at temperatures close to that of gasifier outlet. 151 The expectations of a catalyst material for tar cracking are summarized as follows: 152 1. Good activity and efficiency in removing tar present in a gas mixture (producer gas) 2.…”
Section: Chemical Methods Of Gas Cleaning 421 Thermal and Steammentioning
confidence: 99%
“…Tar reduction using a catalyst is another promising technique, which can be implemented in two ways: one way is integrating the catalyst with the input biomass to eliminate the tar within the gasifier itself (in situ approach), leading to what’s known as catalytic gasification or pyrolysis, and the second way is where tar is removed outside the gasifier in a secondary reactor packed with the catalyst. , Catalysts are effective in cracking tar compounds through reforming, cracking, hydrogenation, and selective oxidation, and many researchers have widely studied their performance over time. ,,,,− Catalytic tar cracking is considered to be promising, as it can be performed at temperatures close to that of gasifier outlet . The expectations of a catalyst material for tar cracking are summarized as follows: Good activity and efficiency in removing tar present in a gas mixture (producer gas) Good stability to deactivation and poisoning Easy regeneration Good abrasive strength Inexpensive and ready availability Less harm to the environment …”
Section: Tar Destruction/removal:
Existing Technologiesmentioning
confidence: 99%
“…58 , 139 Catalysts are effective in cracking tar compounds through reforming, cracking, hydrogenation, and selective oxidation, and many researchers have widely studied their performance over time. 27 , 68 , 70 , 115 , 140 − 151 Catalytic tar cracking is considered to be promising, as it can be performed at temperatures close to that of gasifier outlet. 151 The expectations of a catalyst material for tar cracking are summarized as follows: 152 Good activity and efficiency in removing tar present in a gas mixture (producer gas) Good stability to deactivation and poisoning Easy regeneration Good abrasive strength Inexpensive and ready availability Less harm to the environment …”
Section: Tar Destruction/removal:
Existing Technologiesmentioning
confidence: 99%
“…Based on the nature of impurities, such as halides, siloxanes, etc., sintering, deactivation, and blocking of active sites of catalysts can occur. Although Ni is preferred due to its low cost and wide availability, 151 Ni catalysts (prereduced) are known for being poisoned by sulfides, metal chlorides, and alkali oxides, with reports of rapid deactivation from sulfur and high tar contents due to chemisorption. This could necessitate pretreatment of feed gas, which is not fulfilling the objective of catalytic tar cracking.…”
Section: Tar Destruction/removal:
Existing Technologiesmentioning
Gasification is an advanced thermochemical process that converts carbonaceous feedstock into syngas, a mixture of hydrogen, carbon monoxide, and other gases. However, the presence of tar in syngas, which is composed of higher molecular weight aromatic hydrocarbons, poses significant challenges for the downstream utilization of syngas. This Review offers a comprehensive overview of tar from gasification, encompassing gasifier chemistry and configuration that notably impact tar formation during gasification. It explores the concentration and composition of tar in the syngas and the purity of syngas required for the applications. Various tar removal methods are discussed, including mechanical, chemical/catalytic, and plasma technologies. The Review provides insights into the strengths, limitations, and challenges associated with each tar removal method. It also highlights the importance of integrating multiple techniques to enhance the tar removal efficiency and syngas quality. The selection of an appropriate tar removal strategy depends on factors such as tar composition, gasifier operating and design factors, economic considerations, and the extent of purity required at the downstream application. Future research should focus on developing cleaning strategies that consume less energy and cause a smaller environmental impact.
“…27,68,70,115,140−151 Catalytic tar cracking is considered to be promising, as it can be performed at temperatures close to that of gasifier outlet. 151 The expectations of a catalyst material for tar cracking are summarized as follows: 152 1. Good activity and efficiency in removing tar present in a gas mixture (producer gas) 2.…”
Section: Chemical Methods Of Gas Cleaning 421 Thermal and Steammentioning
confidence: 99%
“…Tar reduction using a catalyst is another promising technique, which can be implemented in two ways: one way is integrating the catalyst with the input biomass to eliminate the tar within the gasifier itself (in situ approach), leading to what’s known as catalytic gasification or pyrolysis, and the second way is where tar is removed outside the gasifier in a secondary reactor packed with the catalyst. , Catalysts are effective in cracking tar compounds through reforming, cracking, hydrogenation, and selective oxidation, and many researchers have widely studied their performance over time. ,,,,− Catalytic tar cracking is considered to be promising, as it can be performed at temperatures close to that of gasifier outlet . The expectations of a catalyst material for tar cracking are summarized as follows: Good activity and efficiency in removing tar present in a gas mixture (producer gas) Good stability to deactivation and poisoning Easy regeneration Good abrasive strength Inexpensive and ready availability Less harm to the environment …”
Section: Tar Destruction/removal:
Existing Technologiesmentioning
confidence: 99%
“…58 , 139 Catalysts are effective in cracking tar compounds through reforming, cracking, hydrogenation, and selective oxidation, and many researchers have widely studied their performance over time. 27 , 68 , 70 , 115 , 140 − 151 Catalytic tar cracking is considered to be promising, as it can be performed at temperatures close to that of gasifier outlet. 151 The expectations of a catalyst material for tar cracking are summarized as follows: 152 Good activity and efficiency in removing tar present in a gas mixture (producer gas) Good stability to deactivation and poisoning Easy regeneration Good abrasive strength Inexpensive and ready availability Less harm to the environment …”
Section: Tar Destruction/removal:
Existing Technologiesmentioning
confidence: 99%
“…Based on the nature of impurities, such as halides, siloxanes, etc., sintering, deactivation, and blocking of active sites of catalysts can occur. Although Ni is preferred due to its low cost and wide availability, 151 Ni catalysts (prereduced) are known for being poisoned by sulfides, metal chlorides, and alkali oxides, with reports of rapid deactivation from sulfur and high tar contents due to chemisorption. This could necessitate pretreatment of feed gas, which is not fulfilling the objective of catalytic tar cracking.…”
Section: Tar Destruction/removal:
Existing Technologiesmentioning
Gasification is an advanced thermochemical process that converts carbonaceous feedstock into syngas, a mixture of hydrogen, carbon monoxide, and other gases. However, the presence of tar in syngas, which is composed of higher molecular weight aromatic hydrocarbons, poses significant challenges for the downstream utilization of syngas. This Review offers a comprehensive overview of tar from gasification, encompassing gasifier chemistry and configuration that notably impact tar formation during gasification. It explores the concentration and composition of tar in the syngas and the purity of syngas required for the applications. Various tar removal methods are discussed, including mechanical, chemical/catalytic, and plasma technologies. The Review provides insights into the strengths, limitations, and challenges associated with each tar removal method. It also highlights the importance of integrating multiple techniques to enhance the tar removal efficiency and syngas quality. The selection of an appropriate tar removal strategy depends on factors such as tar composition, gasifier operating and design factors, economic considerations, and the extent of purity required at the downstream application. Future research should focus on developing cleaning strategies that consume less energy and cause a smaller environmental impact.
“…The reactor was then fitted inside a furnace and connected to a water pump. The catalysts were not reduced prior to the reforming reactions as the activity of both calcined and reduced catalysts converges (unless there are impurities such as H 2 S) due to the formation of similar active sites. , Figure S1 shows the schematic diagram of the steam reforming system. For each run, the reaction conditions were identical: 800 °C, heating rate of 10 °C min –1 , flow rate of pyrolysis gas of 30 mL min –1 (space velocity of 60 mL min –1 g –1 ), and water flow rate of 0.2 g min –1 .…”
Pyrolysis gas from polyolefinic plastic waste is a hydrocarbon-rich
feedstock for sustainable syngas production. The effect of Cr, Mo,
and W promoters on the activity of gasification slag-supported Ni
catalysts during the reforming of plastic pyrolysis gas was investigated
(polyethylene and polypropylene mixed feedstock, Ni:promoter molar
ratio = 4.5, 800 °C, steam-to-carbon molar ratio of 7). Based
on 3 h reforming tests, all catalysts showed stable conversion efficiency,
suggesting that gasification slag from municipal solid waste is a
promising replacement material for traditionally used alumina supports.
Moreover, the slag demonstrated good thermal stability and potential
for catalyst recycling, justifying the economic benefit of valorizing
the material. Interestingly, interaction between slags and promoters
is evidenced by the formation of CaWO4 and CaMoO4 phases, which may have an impact on the reforming activity of bimetallic
catalysts. Among the studied catalysts, the highest conversion efficiency
of hydrocarbon compounds (76%), highest H2 (122.65 mmol
Lfeed
–1) and CO (49.34 mmol Lfeed
–1) yields, and lowest coke deposition (0.06 wt
%) were demonstrated by the Ni–Mo catalyst. The superior performance
of Ni–Mo was accompanied by the growth of carbon nanotubes
via a tip-growth mechanism, which was not observed in other catalysts.
Spherical carbon nanocages and filamentous carbon nanofibers predominated
in coke deposits of Ni, Ni–W, and Ni–Cr. The high syngas
production efficiency of Ni–Mo could be attributed to the dispersion
of metal by the growing carbon nanotubes providing the reaction sites
for reforming and coke gasification reactions. Owing to these properties,
Ni catalyst promoted by Mo and loaded on a gasification support has
high potential for the syngas production from plastic pyrolysis gas.
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