The pyrolysis oil may be a crude pyrolysis oil and may be produced by pyrolysis of biomass material.
The washed biomass is pyrolyzed in a pyrolysis process to form a pyrolysis vapor stream.
Pyrolysis processes can be categorized as slow pyrolysis or fast pyrolysis.
Pyrolysisprocesses can be categorized as slow pyrolysis or fast pyrolysis.
In a final aspect, the invention relates to a process for pyrolysis using such system for pyrolysis.
Waste tarry residues (excluding asphalt cements) arising from refining, distillation and any pyrolitic treatment of organic materials
Y11 Waste tarry residues arising from refining, distillation and any pyrolytic treatment
Prior to pyrolysis, said end of the contact wires is coated with a liquid, which contains a precursor that is converted into a ceramic during the pyrolytic process.
Throughout the pyrolytic process, the door remains locked for total safety.
You can delay the start of the pyrolytic process for
The raw material (12) is degassed in the pyrolysis unit (14) and is converted to the pyrolysis products.
The invention also relates to a novel pyrolysis reactor and to an elementary analyser containing said pyrolysis reactor.
The present invention discloses a pyrolysis unit that operates using a plasma pyrolysis reactor.
The pyrolysis reactor pyrolyzes biomass in the presence of reduced metal oxide sorbents producing char and pyrolysis oil vapor.
The invention relates to a method of carrying out pyrolysis process in a pyrolysis reactor (4) for solid fuel to produce pyrolysis oil.
The present invention provides pyrolysis products that have greater stability than pyrolysis products obtained from conventional pyrolysis production processes.
Further, according to other embodiments, fast pyrolysis processes include open-core fixed bed pyrolysis, ablative fast pyrolysis, cyclonic fast pyrolysis, and rotating core fast pyrolysis systems.
Deposits form adjacent to a pyrolysis oil outlet of the pyrolysis oil stream.
Pyrolysing the evaporated waste generates pyrogas which is burned of as it is generated.
The invention relates to upgraded pyrolysis products, processes for upgrading products obtained from hydrocarbon pyrolysis, equipment useful for such processes, and the use of upgraded pyrolysis products.
A pyrolysis process is provided.
The temperature of the pyrolysis furnace is 450-550℃, the outlet temperature of pyrolysis gas is more than 450℃, therefore, mesothermal pyrolysis is achieved.
During catalytic cracking, the pyrolysis oil deposits adjacent the pyrolysis oil outlet of the pyrolysis oil stream are removed, such as with a cleaning head.
In one embodiment, a method of processing pyrolysis fuel converts biomass to pyrolysis fuel including pyrolysis oil and char particles.
A lower reaction zone is configured to optimize pyrolysis of the biomass into pyrolysis products, while an upper reaction zone is configured to efficiently crack the pyrolysis products.
Requêtes fréquentes français :1-200, -1k, -2k, -3k, -4k, -5k, -7k, -10k, -20k, -40k, -100k, -200k, -500k, -1000k,
Requêtes fréquentes anglais :1-200, -1k, -2k, -3k, -4k, -5k, -7k, -10k, -20k, -40k, -100k, -200k, -500k, -1000k,
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