To enable a carbonized material production kiln to be maintained in a simple manner when an exposed surface on a side wall of the kiln is cracked, to prevent the kiln from easily cracking by heat to thereby prolong the life of the kiln itself, and to increase heat retention efficiency to thereby increase carbonization efficiency even during periods of cold temperatures such as the winter season. The carbonized material production kiln is formed by stacking cubic concrete blocks each having no reinforcing iron so that recombination of up to six faces of each cubic concrete block becomes possible, wherein a heat storage/retention member such as stones is filled in an exhaust space formed between a kiln floor iron plate and a kiln bottom so as to store heat, thereby preventing a decrease in carbonization efficiency even at cold temperatures.

To enable a carbonized material production kiln to be maintained in a simple manner when an exposed surface on a side wall of the kiln is cracked, to prevent the kiln from easily cracking by heat to thereby prolong the life of the kiln itself, and to increase heat retention efficiency to thereby increase carbonization efficiency even during periods of cold temperatures such as the winter season. The carbonized material production kiln is formed by stacking cubic concrete blocks each having no reinforcing iron so that recombination of up to six faces of each cubic concrete block becomes possible, wherein a heat storage/retention member such as stones is filled in an exhaust space formed between a kiln floor iron plate and a kiln bottom so as to store heat, thereby preventing a decrease in carbonization efficiency even at cold temperatures.

The invention relates to a process for converting hydrocarbons into unsaturated products such as acetylene and/or ethylene. The invention also relates to converting acetylene to olefins such as ethylene and/or propylene, to polymerizing the olefins, and to equipment useful for these processes.

The invention relates to a process for converting hydrocarbons into unsaturated products such as acetylene and/or ethylene. The invention also relates to converting acetylene to olefins such as ethylene and/or propylene, to polymerizing the olefins, and to equipment useful for these processes.

A method and process is described for producing negative carbon fuel. In its broadest form, a carbon-containing input is converted to combustible fuels, refinery feedstock, or chemicals and a carbonaceous solid concurrently in separate and substantially uncontaminated form. In an embodiment of the invention, biomass is converted via discrete increasing temperatures under pressure to blendable combustible fuels and a carbonaceous solid. The carbonaceous solid may be reacted to synthesis gas, sold as charcoal product, carbon credits, used for carbon offsets, or sequestered.

A method and process is described for producing negative carbon fuel. In its broadest form, a carbon-containing input is converted to combustible fuels, refinery feedstock, or chemicals and a carbonaceous solid concurrently in separate and substantially uncontaminated form. In an embodiment of the invention, biomass is converted via discrete increasing temperatures under pressure to blendable combustible fuels and a carbonaceous solid. The carbonaceous solid may be reacted to synthesis gas, sold as charcoal product, carbon credits, used for carbon offsets, or sequestered.

Various biomass reactors systems and methods of pyrolyzing biomass are disclosed. One type of biomass reactor system comprises a plurality of biomass processing stations configured in series, each station comprising an auger reactor including an auger inlet for receiving biomass and a transfer screw for conveying the biomass through the auger reactor.

Various biomass reactors systems and methods of pyrolyzing biomass are disclosed. One type of biomass reactor system comprises a plurality of biomass processing stations configured in series, each station comprising an auger reactor including an auger inlet for receiving biomass and a transfer screw for conveying the biomass through the auger reactor.

An apparatus pyrolyzes waste plastics into fuel. The apparatus categorizes the waste plastic, and processes the categorized waste plastic to obtain kerosene, diesel fuel, gasoline etc. The apparatus includes a first heat exchange tank, a rough fuel storage tank, a second heat exchange tank, a diesel storage tank, and a kerosene storage tank. Combustible gas is extracted from the tanks via outlets thereof and stored in a gas storage tank. The combustible gas stored in the gas storage tank is fed into a combustion chamber of a pyrolysis furnace of the apparatus. A fuel-water separate tank is connected to the bottom of the rough fuel storage tank to separate fuel from water. The separated fuel is recycled into the combustion chamber to be burned again. Recycled paper with residual plastic films thereon has to be compressed into grains to facilitate a feeding operation.

An apparatus pyrolyzes waste plastics into fuel. The apparatus categorizes the waste plastic, and processes the categorized waste plastic to obtain kerosene, diesel fuel, gasoline etc. The apparatus includes a first heat exchange tank, a rough fuel storage tank, a second heat exchange tank, a diesel storage tank, and a kerosene storage tank. Combustible gas is extracted from the tanks via outlets thereof and stored in a gas storage tank. The combustible gas stored in the gas storage tank is fed into a combustion chamber of a pyrolysis furnace of the apparatus. A fuel-water separate tank is connected to the bottom of the rough fuel storage tank to separate fuel from water. The separated fuel is recycled into the combustion chamber to be burned again. Recycled paper with residual plastic films thereon has to be compressed into grains to facilitate a feeding operation.