A double fluidized bed reactor system including a staircase-type helical blade is proposed. The system includes a bubbling fluidized bed gasification furnace for receiving fuel (for example, combustible waste and biomass) and steam, forming a bubbling fluidized bed through a flow of flow medium therein, and gasifying the fuel, thereby generating a resultant gas, and a high-speed fluidized bed combustion furnace for receiving char of the resultant gas and the flow medium from the bubbling fluidized bed gasification furnace, additionally receiving air, combusting the char so as to heat the flow medium, and transferring the heated flow medium back to the bubbling fluidized bed gasification furnace.

A double fluidized bed reactor system including a staircase-type helical blade is proposed. The system includes a bubbling fluidized bed gasification furnace for receiving fuel (for example, combustible waste and biomass) and steam, forming a bubbling fluidized bed through a flow of flow medium therein, and gasifying the fuel, thereby generating a resultant gas, and a high-speed fluidized bed combustion furnace for receiving char of the resultant gas and the flow medium from the bubbling fluidized bed gasification furnace, additionally receiving air, combusting the char so as to heat the flow medium, and transferring the heated flow medium back to the bubbling fluidized bed gasification furnace.

A waste treatment incinerator includes a furnace and a microwave transmitting module. The furnace includes a housing defining a treatment space. The furnace includes an activated charcoal layer located in the treatment space. An exhaust pipe is connected to the activated charcoal layer. The microwave transmitting module aligned with the activated charcoal layer. Treatment equipment includes the waste treatment incinerator, a heat exchange system, and a purification module. The heat exchange system includes a first heat exchange module connected to the exhaust pipe of the furnace and a reservoir connected to the first heat exchange module. The purification module includes a gas inlet and a gas outlet. The gas inlet intercommunicates with the first heat exchange module. A sprinkling area is disposed between the gas inlet and the gas outlet.

A waste treatment incinerator includes a furnace and a microwave transmitting module. The furnace includes a housing defining a treatment space. The furnace includes an activated charcoal layer located in the treatment space. An exhaust pipe is connected to the activated charcoal layer. The microwave transmitting module aligned with the activated charcoal layer. Treatment equipment includes the waste treatment incinerator, a heat exchange system, and a purification module. The heat exchange system includes a first heat exchange module connected to the exhaust pipe of the furnace and a reservoir connected to the first heat exchange module. The purification module includes a gas inlet and a gas outlet. The gas inlet intercommunicates with the first heat exchange module. A sprinkling area is disposed between the gas inlet and the gas outlet.

A method for producing valuable organic liquid from a biomass wherein a heated gas is mixed with a biomass to produce an enriched organic vapor and a biomass waste product. The biomass waste product is separated from the enriched organic vapor. The enriched organic vapor is cooled to produce a liquid organic oil and the liquid organic oil is collected. A system for producing the liquid organic oil including a first separation unit to separate an enriched organic vapor and a biomass waste product. The enriched organic vapor and the biomass waste product are generated from mixing a heated gas and a biomass. The system also includes a wet scrubber for cooling the enriched organic vapor to generate an enriched organic smoke. The organic smoke can be transformed to the liquid organic oil in an electrostatic precipitator.

A method for producing valuable organic liquid from a biomass wherein a heated gas is mixed with a biomass to produce an enriched organic vapor and a biomass waste product. The biomass waste product is separated from the enriched organic vapor. The enriched organic vapor is cooled to produce a liquid organic oil and the liquid organic oil is collected. A system for producing the liquid organic oil including a first separation unit to separate an enriched organic vapor and a biomass waste product. The enriched organic vapor and the biomass waste product are generated from mixing a heated gas and a biomass. The system also includes a wet scrubber for cooling the enriched organic vapor to generate an enriched organic smoke. The organic smoke can be transformed to the liquid organic oil in an electrostatic precipitator.

An accumulator is an accumulator disposed between an evaporator and a refrigerant suction port of a compressor in a refrigerant circuit of a refrigeration cycle apparatus. The accumulator includes: a container; an inflow pipe having a first opening end disposed in the container, the inflow pipe introducing, into the container, refrigerant flowing out from the evaporator; and an outflow pipe having a second opening end disposed in the container, the outflow pipe supplying refrigerant in the container to the compressor. The container includes an inner circumferential surface that extends along a vertical direction and a circumferential direction, and a concave surface that is concave with respect to the inner circumferential surface and extends along the circumferential direction. A part of the concave surface in the circumferential direction is disposed to face the first opening end.

An accumulator is an accumulator disposed between an evaporator and a refrigerant suction port of a compressor in a refrigerant circuit of a refrigeration cycle apparatus. The accumulator includes: a container; an inflow pipe having a first opening end disposed in the container, the inflow pipe introducing, into the container, refrigerant flowing out from the evaporator; and an outflow pipe having a second opening end disposed in the container, the outflow pipe supplying refrigerant in the container to the compressor. The container includes an inner circumferential surface that extends along a vertical direction and a circumferential direction, and a concave surface that is concave with respect to the inner circumferential surface and extends along the circumferential direction. A part of the concave surface in the circumferential direction is disposed to face the first opening end.

A crankcase ventilation system comprises a housing defining an internal volume structured to receive a. rotating air/oil separator element. The housing has a housing inlet structured to receive a fluid and a housing outlet defined tangentially in a sidewall of the housing which is structured to allow the fluid to exit the housing. An outlet conduit is fluidly coupled to housing outlet. The outlet conduit comprises an outlet conduit first portion axially aligned with the housing outlet, and an outlet conduit second portion positioned downstream of the outlet, conduit first, portion. A swirl breaking structure is positioned in at least one of an outlet conduit inlet and the outlet conduit second portion. The swirl breaking structure is configured to disrupt swirling flow of the fluid into the outlet conduit so as to reduce a pressure drop experienced by the fluid as the fluid flows from the housing into the outlet conduit.

A crankcase ventilation system comprises a housing defining an internal volume structured to receive a. rotating air/oil separator element. The housing has a housing inlet structured to receive a fluid and a housing outlet defined tangentially in a sidewall of the housing which is structured to allow the fluid to exit the housing. An outlet conduit is fluidly coupled to housing outlet. The outlet conduit comprises an outlet conduit first portion axially aligned with the housing outlet, and an outlet conduit second portion positioned downstream of the outlet, conduit first, portion. A swirl breaking structure is positioned in at least one of an outlet conduit inlet and the outlet conduit second portion. The swirl breaking structure is configured to disrupt swirling flow of the fluid into the outlet conduit so as to reduce a pressure drop experienced by the fluid as the fluid flows from the housing into the outlet conduit.