Embodiments of the present disclosure provide a natural gas separation device, the device comprising a tank, providing with an air inlet, an exhaust port, and a liquid discharge port; a liquid separation assembly, disposed in the tank and dividing an internal space of the tank into a front separation chamber and a liquid recovery chamber, the liquid separation assembly being provided with a liquid return channel for connecting the front separation chamber and the liquid recovery chamber; and a solid separation assembly, disposed in the front separation chamber and connected to the liquid separation assembly.

A dust collector including a cylindrical cyclone tube, a central outlet channel, a swirl generator, and a swirl reflector is disclosed. The cylindrical cyclone tube can include one or more inlets. The central outlet channel includes a lower inlet end and an upper outlet end, wherein the upper outlet end is located above the one or more inlets. The swirl generator can be configured to generate a swirl between the cylindrical cyclone tube and the central outlet channel, the swirl generator configured to encircle the central outlet channel. The swirl reflector can be located near a bottom of the cylindrical cyclone tube and forming a particle chamber there below. A distance between the swirl reflector and the lower inlet end of the central outlet channel can be between ten to fifty percent of the length of the cylindrical cyclone tube from the one or more inlets to the swirl reflector.

A dust collector including a cylindrical cyclone tube, a central outlet channel, a swirl generator, and a swirl reflector is disclosed. The cylindrical cyclone tube can include one or more inlets. The central outlet channel includes a lower inlet end and an upper outlet end, wherein the upper outlet end is located above the one or more inlets. The swirl generator can be configured to generate a swirl between the cylindrical cyclone tube and the central outlet channel, the swirl generator configured to encircle the central outlet channel. The swirl reflector can be located near a bottom of the cylindrical cyclone tube and forming a particle chamber there below. A distance between the swirl reflector and the lower inlet end of the central outlet channel can be between ten to fifty percent of the length of the cylindrical cyclone tube from the one or more inlets to the swirl reflector.

An adaptive spray cleaning system includes a gas tunnel having a gas inlet and a gas outlet. A sprayer assembly is between the gas inlet and the gas outlet. The sprayer assembly includes at least one sprayer array having at least one spray nozzle. The at least one spray nozzle is directed into the gas tunnel. The sprayer assembly includes at least one variable spray configuration characteristic. A sprayer assembly control system is coupled with the at least one sprayer array. The sprayer assembly control system includes one or more sensors proximate at least one of the gas inlet or the gas outlet. The one or more sensors are configured to measure a pollutant characteristic. A controller is in communication with the one or more sensors and the sprayer assembly. The controller is configured to control the at least one variable spray configuration characteristic according to the measured pollutant characteristic.

An adaptive spray cleaning system includes a gas tunnel having a gas inlet and a gas outlet. A sprayer assembly is between the gas inlet and the gas outlet. The sprayer assembly includes at least one sprayer array having at least one spray nozzle. The at least one spray nozzle is directed into the gas tunnel. The sprayer assembly includes at least one variable spray configuration characteristic. A sprayer assembly control system is coupled with the at least one sprayer array. The sprayer assembly control system includes one or more sensors proximate at least one of the gas inlet or the gas outlet. The one or more sensors are configured to measure a pollutant characteristic. A controller is in communication with the one or more sensors and the sprayer assembly. The controller is configured to control the at least one variable spray configuration characteristic according to the measured pollutant characteristic.

A detection device comprises a cyclone-type collection part for collecting particles contained in a gas into a collection liquid with a swirling airflow, a detection part for detecting the particles collected by the cyclone-type collection part; and a cleaning part for cleaning the cyclone-type collection part with a cleaning liquid. The cleaning part cleans the cyclone-type collection part by swirling the cleaning liquid with the swirling airflow generated in the cyclone-type collection part.

A detection device comprises a cyclone-type collection part for collecting particles contained in a gas into a collection liquid with a swirling airflow, a detection part for detecting the particles collected by the cyclone-type collection part; and a cleaning part for cleaning the cyclone-type collection part with a cleaning liquid. The cleaning part cleans the cyclone-type collection part by swirling the cleaning liquid with the swirling airflow generated in the cyclone-type collection part.

Process and apparatus capable to remove particles from a fluid stream (such as air or water) and directly convert the removed particles into a solid compact format commonly known as briquettes in a standalone combined single unit operation. The outlined process and equipment operates without the need for rotary valve technology and uses air versus hydraulics offering a cost competitive equipment solution for the end user. Active processes within the apparatus actively control the dust thereby allowing a variety of particles to be processes irrespective of moisture content and surface adhesive characteristics. Having the low-cost capability to convert explosive air/dust mixtures into briquettes significantly enhances safety and also reduces the associated manhandling effort required with disposing of collected dust with many briquettes typically having 100-500 the density of the incoming particles. In many regions the produced briquettes have a second hand value thereby creating a value stream from a zero value dust stream.

Process and apparatus capable to remove particles from a fluid stream (such as air or water) and directly convert the removed particles into a solid compact format commonly known as briquettes in a standalone combined single unit operation. The outlined process and equipment operates without the need for rotary valve technology and uses air versus hydraulics offering a cost competitive equipment solution for the end user. Active processes within the apparatus actively control the dust thereby allowing a variety of particles to be processes irrespective of moisture content and surface adhesive characteristics. Having the low-cost capability to convert explosive air/dust mixtures into briquettes significantly enhances safety and also reduces the associated manhandling effort required with disposing of collected dust with many briquettes typically having 100-500 the density of the incoming particles. In many regions the produced briquettes have a second hand value thereby creating a value stream from a zero value dust stream.

A surface cleaning apparatus including an air treatment unit, a refuse unit, and a flexible hose. The air treatment unit includes an air flow path from a dirty air inlet to a clean air outlet and an air treatment member comprising an air treatment chamber and a dirt collection region having an emptying door which is operable between a closed position and an open position. The flexible hose is removably connectable to the dirty air inlet. The air treatment unit is operable in a first operating mode in which the air treatment member is in air flow communication with the dirty air inlet and the emptying door is closed. The air treatment unit is operable in a second operating mode in which air flow through the air treatment member is terminated and the emptying door is open whereby dirt is transferable to a refuse container of the refuse unit.