Patent classifications
C10B53/02
METHOD FOR PRODUCING A BIOFUEL BY STEAM CRACKING
A method for producing a biofuel by continuous or discontinuous steam cracking of lignocellulosic biomass, comprises: —recording a digital model of the optimal steam cracking parameters as a function of the typology of the plant constituents of the biomass; —supplying the steam cracking reactor with heterogeneous biomass; —measuring at least once during the treatment the typology of the plant constituents of the biomass; and —controlling the adjustment of the steam cracking parameters as a function of the typology of the plant constituents of the measured biomass and of the digital model.
INTEGRATED PYROLYSIS AND GASIFICATION OF BIOMASS
Systems and methods are provided for integrated pyrolysis and gasification of a biomass feed, either as a separate feed or under co-processing conditions. The integrated pyrolysis and gasification can be performed using any convenient reactor configuration, such as fluidized coking reactor configuration or a fluid catalytic cracking reactor configuration. The biomass feed can initially by pyrolyzed to form liquid products, gas phase products, and char. The char can then be used as the input feed to gasification. In aspects where the biomass feed is co-processed, the biomass can be co-processed with a co-feed that is suitable for processing under fluidized coking conditions or other pyrolysis conditions, such as a conventional fluidized coking feedstock.
FLUIDIZED BED REACTOR SYSTEMS AND METHODS FOR TORREFACTION AND CATALYTIC PYROLYSIS OF BIOMASS
A fluidized bed reactor for biomass treatment comprising a vessel extending in a first direction from a first end to a second end, an inlet at the first end of the vessel for feeding biomass particles into the vessel, an outlet at the second end of the vessel for outputting processed biomass, a first fluid inlet independently activatable to deliver a first volume of a gas in a second direction into a first region of the vessel, and a second fluid inlet spaced apart from the first fluid inlet in the first direction and independently activatable to deliver a second volume of the gas in the second direction into a second region of the vessel, the second region adjacent the first region.
FEEDSTOCK PROCESSING METHOD AND SYSTEM
The invention relates to a process, method and devices for recovery of products from a feedstock such as an organic, non-organic or biodynamic feedstock. The products include consumables such as high nutrition foods, nutraceuticals and bioactive compounds and/or non-consumables such as energy and synfuels. The invention typically includes real-time process optimisation. The devices include a counter current diffusion extractor and a decorticator for deriving useful products from a feedstock, optionally for consumption in further processing.
FEEDSTOCK PROCESSING METHOD AND SYSTEM
The invention relates to a process, method and devices for recovery of products from a feedstock such as an organic, non-organic or biodynamic feedstock. The products include consumables such as high nutrition foods, nutraceuticals and bioactive compounds and/or non-consumables such as energy and synfuels. The invention typically includes real-time process optimisation. The devices include a counter current diffusion extractor and a decorticator for deriving useful products from a feedstock, optionally for consumption in further processing.
PROCESS TO PREPARE A GAS OIL PRODUCT
The invention is directed to a process to prepare a gas oil product from a carbonaceous particles of a biomass source comprising the following steps: (a) pyrolysis of the carbonaceous particles to a gaseous mixture of hydrocarbons in the absence of oxygen, (b) quenching the gaseous mixture of hydrocarbons by contacting with a liquid quench mixture of hydrocarbons having a lower temperature than the gaseous mixture thereby obtaining a rich liquid quench mixture and a quenched gas, and (c) isolating from the quenched gas a gas oil product by means of vacuum distillation, wherein the liquid gas oil is partly supplied to the top of the vacuum distillation column as a distillation reflux, partly used as part of the liquid quench mixture in (b) and partly discharged as the gas oil product.
PROCESS TO PREPARE A GAS OIL PRODUCT
The invention is directed to a process to prepare a gas oil product from a carbonaceous particles of a biomass source comprising the following steps: (a) pyrolysis of the carbonaceous particles to a gaseous mixture of hydrocarbons in the absence of oxygen, (b) quenching the gaseous mixture of hydrocarbons by contacting with a liquid quench mixture of hydrocarbons having a lower temperature than the gaseous mixture thereby obtaining a rich liquid quench mixture and a quenched gas, and (c) isolating from the quenched gas a gas oil product by means of vacuum distillation, wherein the liquid gas oil is partly supplied to the top of the vacuum distillation column as a distillation reflux, partly used as part of the liquid quench mixture in (b) and partly discharged as the gas oil product.
BIOCHAR AS A MICROBIAL CARRIER
The invention relates to a microbial delivery system where biochar acts as a carrier for microbes.
BIOCHAR AS A MICROBIAL CARRIER
The invention relates to a microbial delivery system where biochar acts as a carrier for microbes.
BIOMASS PYROLYSIS DEVICE AND METHOD WITH OPTIMIZED MATCHING OF THERMAL ENERGY AND MICROWAVE ENERGY
A biomass pyrolysis device and a biomass pyrolysis method is for optimal matching of thermal energy and microwave energy, wherein the device comprises a power generation system, a drying device and a microwave pyrolysis device; wherein the drying device is a cylinder nested with a flue gas layer and a material layer, a material inlet of the drying device is connected with a feeding device, and a volatile outlet is connected with a condensing unit; the microwave pyrolysis device is connected with a material outlet of the drying device, and a pyrolysis gas outlet of the microwave pyrolysis device is connected with the condensing unit; the condensing unit is connected with the power generation system, and waste gas generated by the power generation system is introduced into the flue gas layer of the drying device.