Some embodiments are directed to a process for forming products from animal waste (e.g., poultry litter). The products may include a controlled release fertilizer and renewable natural gas. The process may include providing a feedstock comprising greater than about 80 percent poultry waste and a moisture content of about 25 percent. The feedstock may be diluted to form a slurry having a moisture content of about 90%. The slurry may be mechanically refined to reduce the particle size distribution and the average particle size of the slurry. The slurry may be anaerobically digested to produce biogas and a digestate. The biogas may be converted to renewable natural gas, and the digestate may be converted to a controlled release fertilizer. Additionally, some embodiments are directed to methods of reducing nitrogen emission from soil amendments. Some embodiments are directed to reducing nitrogen emissions sufficient to produce emissions offset credits.

Used AHP or its components is converted into low molecular weight hydrocarbons using HTT reactor. These low molecular weight hydrocarbons produce ethylene, propylene, and other chemicals when fed into a steam cracker, which can be used to produce recycled components of the AHP or a fully recycled AHP.

This invention relates to the field of contaminated plastic waste decomposition. More specifically, the invention comprises methods and systems to decompose contaminated plastic waste and transform it into value-added products.

This invention relates to the field of contaminated plastic waste decomposition. More specifically, the invention comprises methods and systems to decompose contaminated plastic waste and transform it into value-added products.

The present invention belongs to the field of energy and environmental protection and particularly relates to an organic solid waste treatment device based on chemical-looping hydrogen production and a method for using the same. The device comprises a pyrolysis reactor (3) and a sleeve-type chemical-looping reactor (19), the sleeve-type chemical-looping reactor (19) comprises an inner cavity, an outer cavity annularly wrapping the inner cavity, a syngas output device (28), a hydrogen output device (29), a pyrolysis gas inlet device (6), and a water vapor inlet device (7), and the pyrolysis reactor (3) can generate pyrolysis gas, which then is conveyed to the sleeve-type chemical-looping reactor (19) through the pyrolysis gas inlet device (6). By designing the chemical-looping reforming coupling hydrogen production continuous reaction device in the present invention, chemical-looping reforming and chemical-looping hydrogen production technologies can be realized in one process, co-production of syngas and high-concentration hydrogen can be realized without a complicated gas separation and purification system for hydrogen, the cost is low, and the operation is simple.

The present invention belongs to the field of energy and environmental protection and particularly relates to an organic solid waste treatment device based on chemical-looping hydrogen production and a method for using the same. The device comprises a pyrolysis reactor (3) and a sleeve-type chemical-looping reactor (19), the sleeve-type chemical-looping reactor (19) comprises an inner cavity, an outer cavity annularly wrapping the inner cavity, a syngas output device (28), a hydrogen output device (29), a pyrolysis gas inlet device (6), and a water vapor inlet device (7), and the pyrolysis reactor (3) can generate pyrolysis gas, which then is conveyed to the sleeve-type chemical-looping reactor (19) through the pyrolysis gas inlet device (6). By designing the chemical-looping reforming coupling hydrogen production continuous reaction device in the present invention, chemical-looping reforming and chemical-looping hydrogen production technologies can be realized in one process, co-production of syngas and high-concentration hydrogen can be realized without a complicated gas separation and purification system for hydrogen, the cost is low, and the operation is simple.

In this treatment method of a coated wire, a coated wire, which is a metal wire coated with a resin, is subjected to low-temperature heating in a non-combustion atmosphere in coexistence with an alkali to embrittle the coating resin, the embrittled coating resin is crushed, and the coating resin and the metal wire are separated.

The present invention provides a method and a system for processing of waste by anaerobic digestion, said method comprising pre-treatment of a first biological waste stream by thermal hydrolysis and processing of a solid fraction by pyrolysis prior to anaerobic digestion.

The present invention allows for efficient utilization of the energy available in biological waste sources. The method provides an energy efficient method for processing of biological waste having a high degree of recovery of the energy stored in the waste material, wherein the flow of material may be dynamically adjusted to e.g. achieve end products in preferred ratios.

The present invention provides a method and a system for processing of waste by anaerobic digestion, said method comprising pre-treatment of a first biological waste stream by thermal hydrolysis and processing of a solid fraction by pyrolysis prior to anaerobic digestion.

The present invention allows for efficient utilization of the energy available in biological waste sources. The method provides an energy efficient method for processing of biological waste having a high degree of recovery of the energy stored in the waste material, wherein the flow of material may be dynamically adjusted to e.g. achieve end products in preferred ratios.

The invention related to an apparatus for recycling of lignocellulosic fibres from a fibreboard comprising compressed lignocellulosic fibres bonded together by a binding agent. The apparatus comprises a transport device arranged within a closed housing, wherein the housing is arranged for steaming pieces of the fibreboard at super-atmospheric pressure to decompress and release the lignocellulosic fibres by hydrating them, as well as hydrolysing the binding agent, and the transport device is arranged for transporting the fibreboard pieces, upon being steamed, from an inlet of the housing, at which the fibreboard pieces are fed to the housing, to an outlet of the housing, at which steamed portions comprising released lignocellulosic fibres exit the housing. Further, the apparatus comprises a steam generator in communication with the housing, whereby the fibreboard pieces may be steamed at super-atmospheric pressure in the housing to provide the steamed portions comprising released lignocellulosic fibres, an inlet pressure lock configured to receive the fibreboard pieces at atmospheric pressure and to deliver them to the housing, via the inlet, at super-atmospheric pressure, and an outlet pressure lock configured to receive steamed portions comprising released lignocellulosic fibres via the outlet and ejecting recycled lignocellulosic fibres during a sudden expansion of super-atmospheric pressure.