A vapor distributor for use in an internal region of a mass transfer column to receive and redistribute a vapor stream when it is introduced radially into the internal region through a radial inlet in a shell of the mass transfer column. The vapor distributor includes a plurality of multiple-sided elongated deflectors arranged in a descending array and a pair of braces that extend longitudinally across the array of elongated deflectors and hold them in spaced apart and side-by-side relationship to each other. Each of the elongated deflectors has a deflecting surface that faces toward the radial inlet to redirect and redistribute the radially-introduced vapor stream. The braces each include a strut that may also redirect and redistribute the vapor stream.

A separation system for separating constituents from a solution by utilizing a carrier gas and a separation method thereof are disclosed. The separation system includes an evaporator, a solution distribution unit connected to the evaporator for distributing the solution into the evaporator, and a gas distribution unit connected to the evaporator for distributing the carrier gas into the evaporator. The solution is countercurrent to the carrier gas and upon contact, at least one constituent of the solution is vaporized and separated from the solution.

A short path evaporator including a heatable double-walled evaporator pipe having an inner interspace, with a rotatable rotor system disposed within the evaporator pipe and with a condenser disposed centrally in the evaporator pipe, and with an inlet for a product leading into the evaporator pipe, an outlet for a concentrate of the product leading out of the evaporator pipe, and an outlet for distillate accumulating at the condenser, and an inlet and an outlet for supplying and discharging heating medium to or from the interspace of the evaporator pipe, wherein the evaporator pipe is formed by an outer pipe and an inner pipe which, leaving the interspace, is disposed within the outer pipe, which are fixed at their ends in a sealing manner between two flange plates clamped together, wherein an inlet channel for the inlet of the product and an outlet channel for the outlet of the concentrate, which communicate with the interior of the inner pipe, are formed in the flange plates, as well as inlet and outlet channels for supplying and discharging the heating medium, which communicate with the interspace.

Methods and systems involving thermal desorption of an oily slurry are provided. In some embodiments, such systems include a desorption vessel including an inner chamber; a heating unit disposed adjacent to the desorption vessel configured to heat a slurry including solids and oil disposed in the inner chamber of the desorption vessel; and a plurality of vapor outlets in fluid communication with the inner chamber of the desorption vessel, wherein each vapor outlet is in fluid communication with a condenser or an eductor for condensing vapors generated by heating the slurry.

A method for cleaning a vaporizer that vaporizes, at normal temperature and pressure, a source material in a liquid state, and supplies the vaporized source material to a reactor through a supply pipe, includes a cleaning step of passing the source material to the vaporizer while maintaining the source material in a liquid state to clean the vaporizer.

In order to appropriately control temperatures of fluid heating sections that are maintained at different temperatures, the fluid control device (100) comprises a plurality of fluid heating sections (1) connected to each other and each having a flow path or a fluid accommodating portion inside, heaters (10) configured to heat each of the plurality of fluid heating sections to different temperatures, and heat insulating members (13, 13′) disposed between adjacent fluid heating sections.

The present invention generally relates to a system for treating effluent water. More particularly, it provides a robust apparatus for treating waste liquid by optimizing solar and wind energy to maximize the evaporation rate as compare to natural evaporation rate. The main object of the present invention is to provide a system for evaporating RO reject and other effluent liquid and other liquids, by optimizing system to solar and wind energy to maximize vaporization rate and recovery rate at marginal operational cost.

A gas trap assembly including a base connector housing including an inflow port and an outflow port, a reservoir fluidly connecting the inflow port to the outflow port, and a grooved porous media located within the reservoir. The grooved porous media including a plurality of grooves and composed of a material having a plurality of pores of a selected size. The grooved porous media fluidly divides the reservoir into two portions in such a way that a working fluid flowing from the inflow port to the outflow port must flow through the plurality of grooves and the plurality of pores of the grooved porous media. The plurality of grooves and the plurality of pores are configured to prevent gas from passing through the grooved porous media.

An evaporator for submerged combustion and delayed evaporation, a method of the same and a system of combined evaporation devices, the evaporator for submerged combustion and delayed evaporation comprises: a housing formed with a space for containing an evaporating liquid; a separator plate arranged in an interior of the housing and dividing the housing into a heat transfer (submerged combustion) area and an evaporation area; a vapor chamber located above a liquid surface of the evaporation area; a flue gas chamber located above a liquid surface of the heat transfer area, wherein the flue gas chamber is provided with a flue gas outlet, the flue gas outlet is provided with a pressure valve which is capable of controlling a gas pressure within the flue gas chamber such that a gas pressure within the flue gas chamber is larger than a gas pressure within the vapor chamber.

A cyclone-assisted distillation system including an energy supply system configured to generate water vapor; a cyclone-generating device configured to generate a vortex with the water vapor received from the energy supply system, the vortex generating a water vapor jet; and a distillation system configured to generate distillated water from saltwater, based on a steam jet obtained from (1) the water vapor of the energy supply system and (2) the water vapor jet from the cyclone-generating device.