Patent classifications
C10B57/00
Methods and systems to produce needle coke from aromatic recovery complex bottoms
Provided here are systems and methods of production of needle coke by processing an aromatic rejects stream containing long chain alkyl monoaromatics and bridged diaromatics through a delayed coking process. Various other embodiments may be disclosed and claimed.
TORREFIED BIOMASS BRIQUETTES AND RELATED METHODS
The presently disclosed subject matter relates to torrefied biomass briquettes and methods for producing the same that make use of a mixture of lightly torrefied material (LTM) and highly torrefied material (HTM) and/or make use of torrefied materials that are subjected to a hydrolysis pretreatment prior to being torrefied.
TORREFIED BIOMASS BRIQUETTES AND RELATED METHODS
The presently disclosed subject matter relates to torrefied biomass briquettes and methods for producing the same that make use of a mixture of lightly torrefied material (LTM) and highly torrefied material (HTM) and/or make use of torrefied materials that are subjected to a hydrolysis pretreatment prior to being torrefied.
METHOD AND APPARATUS FOR THE MANUFACTURING OF NON-ENERGENT BIOCOAL WITH THERMAL TREATMENT
A method and an apparatus for manufacturing, with thermal treatment, biocoal which is non-energent, such as functional as a heat sink, by using a conveyor arrangement housed in an essentially Thompson Converter type process space. A to-be-processed feedstock is conveyed in the process space with the conveyor arrangement, which is closed relative thereto, in a longitudinal direction of the process space. A pyrolysis gas, generated from the to-be-processed feedstock present inside the conveyor arrangement as a result of heat transferring from the process space thereto, is conducted into a combustion chamber included in the process space for burning the gas, a thereby generated flue gas being removed from the process space by a discharge arrangement and a resulting non-energent biocoal being removed from the conveyor arrangement for further processing.
METHOD OF EVALUATING COAL, METHODS OF PREPARING COAL BLEND, AND METHOD OF PRODUCING COKE
A method of evaluating coal includes preparing coal samples having different inert amounts by pulverizing one brand of coal; measuring the inert amounts of the respective coal samples and measuring surface tensions of semi-coke obtained by heat treating the respective coal samples; and determining a regression line based on the inert amounts and the surface tensions and evaluating the coal by using, as an index, a ratio of a variation in the surface tensions to a variation in the inert amounts as determined from the regression line.
METHOD OF EVALUATING COAL, METHODS OF PREPARING COAL BLEND, AND METHOD OF PRODUCING COKE
A method of evaluating coal includes preparing coal samples having different inert amounts by pulverizing one brand of coal; measuring the inert amounts of the respective coal samples and measuring surface tensions of semi-coke obtained by heat treating the respective coal samples; and determining a regression line based on the inert amounts and the surface tensions and evaluating the coal by using, as an index, a ratio of a variation in the surface tensions to a variation in the inert amounts as determined from the regression line.
Apparatus and method of producing activated carbon material
The present invention relates to an apparatus and a method of producing activated carbon material in a reactor from carbonised material using at least in part the flue gas from another reactor pyrolytically producing the carbonised material from a feed material.
Methods and systems for producing an enhanced surface area biochar product
Herein disclosed are apparatus and associated methods related to producing an enhanced surface area biochar product with a desired activation level based on receiving biochar into a processing vessel configured with multiple independently temperature-controlled chambers and counter-flow steam injection, controlling activation levels of the biochar by moving the biochar through the processing vessel and adjusting the temperature of the biochar by injecting steam into at least one temperature-controlled chamber of the processing vessel, recovering volatiles driven off through dehydration using a thermal oxidizer, cooling the biochar to a desired discharge temperature using steam and retention time, and discharging the activated biochar product. The processing vessel may be a calciner, a rotary calciner, or a kiln. Biochar may be heated or cooled to a desired thermochemical processing temperature depending on the temperature of the received biochar. Counter-flow saturated steam may sweep volatile gases to a thermal oxidizer using a vacuum system.
COMPOSITION AND PROCESS FOR PELLETIZING CARBON-BASED MATERIALS FOR PROPPANT AND INDUSTRIAL APPLICATIONS
A method for producing an electrically-conductive pellet includes reducing a size of a first material. The method also includes wetting the first material to produce a first slurry. The method also includes introducing the first slurry into a fluidizer to produce a first pellet. The method also includes reducing a size of a second material. The second material is an electrically-conductive material. The method also includes wetting the second material to produce a second slurry. The method also includes applying the second slurry to the first pellet.
Pot furnace low-temperature calcination process
A pot furnace low-temperature calcination process may ensure that, by controlling the flame path temperature and discharge speed of the pot furnace, that the range of the temperature at which the petroleum coke is calcined in the pot is from 1150° C. to 1220° C., and that the discharge speed is 10 to 20% higher than the normal discharge speed and reaches 110˜120 kg/h, reducing the amount of desulfurization of the petroleum coke during the calcination so that the true density of the calcined coke is between 2.05 and 2.07 g/cm.sup.3.