There is disclosed a water purification apparatus and method, related to desalinization. In an embodiment, a water purification apparatus and method includes at least one port for receiving airflow therethrough, at least one port for receiving salt water therethrough, at least one output for providing outflow of pure water vapor, and at least one output for proving outflow of a mixture of water, salt and air; and a plurality of chambers for evaporating the salt water into the airflow, at least one of the chambers forming a plurality of ports arranged in a plurality of rows. In an embodiment, a method includes providing airflow to a water purification apparatus; providing salt water to the water purification apparatus and method; forming a vortex in the airflow to evaporate water vapor from the salt water; and providing the water vapor in the airflow to a condenser so as to obtain pure water.

There is disclosed a water purification apparatus and method, related to desalinization. In an embodiment, a water purification apparatus and method includes at least one port for receiving airflow therethrough, at least one port for receiving salt water therethrough, at least one output for providing outflow of pure water vapor, and at least one output for proving outflow of a mixture of water, salt and air; and a plurality of chambers for evaporating the salt water into the airflow, at least one of the chambers forming a plurality of ports arranged in a plurality of rows. In an embodiment, a method includes providing airflow to a water purification apparatus; providing salt water to the water purification apparatus and method; forming a vortex in the airflow to evaporate water vapor from the salt water; and providing the water vapor in the airflow to a condenser so as to obtain pure water.

Condenser-evaporator tube, in whose interior flows a vapor to be condensed and over which flows a liquid to be evaporated, where both inside and outside faces of this tube are covered with capillary structures configured for the formation of liquid menisci having a contact angle smaller than 90? where the liquid-vapor interface curves, which allows capillary condensation inside the tube and evaporation on the outside face at the upper end (25) of the liquid menisci where the liquid layer is thinnest and the evaporation most efficient.

A reboiler in fluid communication with a fractionator column in an offshore low temperature process removing carbon dioxide from natural gas has a vessel volume. A carbon steel tubing bundle is disposed within the vessel volume. Each tube in the bundle has an outer surface with a porous granular metal layer deposited thereon. The granular metal layer comprises a pore size distribution which promotes bubble nucleation during vaporization of a nearly pure liquid carbon dioxide stream.

The present embodiments provide a system and method for separation within a polymer production process. Specifically, a flashline heater configured according to present embodiments may provide more time than is required for complete vaporization of liquid hydrocarbons that are not entrained within a polymer fluff produced within a polymerization reactor. Such extra time may allow for liquid hydrocarbons that are entrained within the polymer fluff to be vaporized.

The present embodiments provide a system and method for separation within a polymer production process. Specifically, a flashline heater configured according to present embodiments may provide more time than is required for complete vaporization of liquid hydrocarbons that are not entrained within a polymer fluff produced within a polymerization reactor. Such extra time may allow for liquid hydrocarbons that are entrained within the polymer fluff to be vaporized.

Mechanical vapor recompression (MVR) liquid purification system includes a pressure-tight enclosure having a circular cylindrical elongated shape along a longitudinal axis A, and evaporation compartments E1-E3 arranged within the enclosure. Each compartment has a plurality of longitudinal pipes running from one sidewall to another sidewall, and circular sidewalls having openings for the plurality of pipes. A central tube runs along the axis A through the centers of the compartments E1-E3, and allows steam to flow from the second end to the first end. The number of pipes is highest in the first compartment E1, then gradually fewer in the second E2 and third E3. The pipes allow steam to flow from the first end to the second end. A compressor assembly includes a compressor provided with compressor vane members structured to provide steam flow along the longitudinal axis and a motor for rotating the compressor at a variable rotational speed.

Mechanical vapor recompression (MVR) liquid purification system includes a pressure-tight enclosure having a circular cylindrical elongated shape along a longitudinal axis A, and evaporation compartments E1-E3 arranged within the enclosure. Each compartment has a plurality of longitudinal pipes running from one sidewall to another sidewall, and circular sidewalls having openings for the plurality of pipes. A central tube runs along the axis A through the centers of the compartments E1-E3, and allows steam to flow from the second end to the first end. The number of pipes is highest in the first compartment E1, then gradually fewer in the second E2 and third E3. The pipes allow steam to flow from the first end to the second end. A compressor assembly includes a compressor provided with compressor vane members structured to provide steam flow along the longitudinal axis and a motor for rotating the compressor at a variable rotational speed.

Techniques are described herein for using a high-pressure reactor to separate clean water from dirty water without filtration and to extract and concentrate contaminants from dirty water for use as a fuel. In particular, techniques and systems are described for separating water from hydrocarbon contaminates, other BTU-laden compounds, and dissolved minerals, while also boiling water and condensing the resulting steam into distilled water. In addition, system in which the described techniques are performed can be used as a high-pressure pump for moving the separated hydrocarbon contaminates forward into other processes, such as a high-pressure reactor or incinerator.

Techniques are described herein for using a high-pressure reactor to separate clean water from dirty water without filtration and to extract and concentrate contaminants from dirty water for use as a fuel. In particular, techniques and systems are described for separating water from hydrocarbon contaminates, other BTU-laden compounds, and dissolved minerals, while also boiling water and condensing the resulting steam into distilled water. In addition, system in which the described techniques are performed can be used as a high-pressure pump for moving the separated hydrocarbon contaminates forward into other processes, such as a high-pressure reactor or incinerator.