A heat and mass transfer system configured to be a passive system using gravitational force to form a thin liquid film flow on an outer surface of a flow distribution head and downstream conduit member to subject the thin liquid film to heat transfer mediums. The at least partially spherical flow distribution head creates a uniform thin flow of liquid on the outer surface increasing the efficiency of the heat and mass transfer system. The heat and mass transfer system may include a heat transfer medium supply system in fluid communication with internal aspects of the downstream conduit such that a heat transfer medium flows within the downstream conduit while the liquid film flows on the outer surface of the downstream conduit. Rather than conventional sheet flow on inner surfaces of a conduit, the flow distribution head enables sheet flow to be formed on an outside surface of a component.

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.

The present disclosure describes an apparatus that may be used to generate desalinated water from a supply of untreated water using a photovoltaic cell. The front surface of the photovoltaic cell is partially enclosed to form an evaporation chamber. The front surface of the photovoltaic cell is exposed to sunlight or another light source. This exposure results in power generation by the photovoltaic cell and also heats the air in the evaporation chamber. Untreated water is subsequently introduced into the evaporation chamber. Upon contacting the heated air and the front surface of the photovoltaic cell, a portion of the untreated water evaporates to generate water vapor. The water vapor is then removed from the evaporation chamber and transported to a condensation chamber. The water vapor is cooled in the condensation chamber to yield desalinated water.

A skid-mounted system, for recycling production salt water from an oil well, may include a skid housing; a separation tank enclosed within the skid housing; a control system enclosed within the skid housing; a salt water port configured to be connected to a supply of salt water and transfer the salt water to the separation tank; a fuel port configured to be connected to a fuel supply and provide fuel to a burner attached to the separation tank; an exhaust stack that is connected to the separation tank and that is configured to exhaust hot gas produced by the burner to an environment; and a steam stack that is connected to the separation tank and that is configured to release steam produced by the separation tank.

The invention concerns an apparatus (10) for separation of components with different volatility in a mixed fluid, said apparatus (10) comprising: a first heat exchanging unit (100) provided with first and second flow path structures (131, 132) forming separate flow paths for a first and a second fluid flow through the first heat-exchanging unit (100); an inlet (118) for feeding the mixed fluid to the apparatus (10); an inlet (119) for feeding steam to the apparatus (10); an arrangement for feeding a cooling medium through the apparatus (10), wherein said arrangement comprises at least one cooling medium inlet (105, 106, 107, 108). The invention is characterized in that the apparatus (10) comprises a second heat-exchanging unit (200) provided with third and fourth flow path structures (233, 234) forming separate flow paths for a first and a second fluid flow through the second heat-exchanging unit (200), wherein the cooling medium arrangement comprises at least one cooling medium inlet (205, 206, 207, 208) arranged in fluid communication with the fourth flow path structure (234) and wherein the first and third flow path structures (131, 233) are arranged in fluid communication with each other.

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.

In accordance with one or more embodiments of the present disclosure, a computer-controlled programmable logic controller (PLC) extraction system for separating an extract from a biomass includes a PLC, a solvent reservoir comprising a solvent that is a gas when the solvent is at a temperature of 25 C. and atmospheric pressure, a plurality of extraction devices comprising the biomass, an extract collection reservoir for collecting the extract, a solvent recovery system, and a temperature controlled circulation system. The circulation system fluidly connects the solvent reservoir, the plurality of extraction devices, the extract collection reservoir, and the solvent recovery system and comprises at least one apparatus for controlling a flow of the solvent. The solvent comprises no more than 1 weight % CO.sub.2. A method of extracting an extract from a biomass using a PLC extraction system is also described.

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.

Systems, apparatuses, and methods for cleaning brine solution are provided. In particular, one or more embodiments comprise a brine cleaning system that includes a brine cooker, a brine filter, and a brine storage unit. The brine cooker heats a dirty brine solution to separate the dirty brine solution into a liquid portion and a solids portion. The brine filter is coupled to the brine cooker to receive the liquid portion and the solids portion from the brine cooker and then substantially remove the solids portion. The brine storage unit is coupled to the brine filter to accumulate the liquid portion once the solids portion have been substantially removed by the brine filter. This allows for more efficient and environmentally friendly use of brine solution in the curing of animal.

An in-line blending process for polymers comprising: (a) providing two or more reactor-low pressure separator units (1,7) in parallel configuration, each reactor-low pressure separator unit comprising one reactor (2,8) fluidly connected to one low pressure separator (3,9) downstream and further a recycling line (5,11) connecting the low pressure separator (3,9) back to the corresponding reactor (2,8); (b) polymerizing olefin monomers having two or more carbon atoms in each of the reactors (2,8) in solution polymerisation; (c) forming an unreduced reactor effluents stream including a homogenous fluid phase polymer-monomer-solvent mixture in each of the reactors (2,8), (d) passing the unreduced reactor effluents streams from each of the reactors (2,8) through the corresponding low pressure separators (3,9), whereby the temperature and pressure of the low pressure separators (3,9) is adjusted such that a liquid phase and a vapour phase are obtained, whereby yielding a polymer-enriched liquid phase and a polymer-lean vapour phase, and (e) separating the polymer-lean vapour phase from the polymer-enriched liquid phase in each of the low-pressure separators (3,9) to form separated polymer-lean vapour streams and separated polymer-enriched liquid streams; (f) combining the polymer-enriched liquid streams from step (e) in a further low-pressure separator and/or a mixer (13) to produce a combined polymer-enriched liquid stream (16); (g) reintroducing the polymer-lean vapour streams from step (e) via recycling lines (5,11) into the corresponding reactors (2,8).