Methods, systems, and techniques for desalinating a saltwater using a humidifier unit. The humidifier unit has a housing, which has a carrier gas inlet and a saltwater inlet. The humidifier unit also includes a packing, within the housing, having a surface with a critical surface tension of less than 25 mN/m according to the Zisman method. The packing is arranged to facilitate a saltwater that enters the housing through the saltwater inlet and a carrier gas that enters the housing through the carrier gas inlet to contact each other. The contact facilitates evaporation of the saltwater, which produces salt solids on at least a surface of the packing, a humidified gas and a concentrated brine.

Provided is a vaporizer capable of reducing the occurrence of bumping in a vaporization space and thereby minimizing the pressure fluctuations therein, when a method not using an atomizer is employed. A vaporizer (1) includes a tank body (10), a porous member (30) disposed in the vaporizer (1) and heated, a supply tube (40) configured to supply a liquid material (L) to the porous member (30), and a gas discharge passage (7) configured to discharge a source gas (G) produced by vaporizing the liquid material (L) to the outside. An outlet (41) of the supply tube (40) is disposed in contact with or in close proximity to the porous member (30). When the outlet (41) is disposed in close proximity to the porous member (30), a separation distance (H) between the outlet (41) and the porous member (30) is not greater than a distance from the outlet (41) to a bottom of a droplet of the liquid material (L) formed and suspended at the outlet (41) by surface tension.

According to one aspect of the invention, a system to separate salt from uranium. The system has a vessel, a heater, a pump, and a condenser. The vessel is adapted to receive a uranium that has a salt concentration. The heater heats the uranium for a period of time, causing the salt to turn into a salt vapor and the uranium to melt. The melted uranium releases the salt vapor. The pump circulates an inert gas that carries the salt vapor away from the melted uranium. The condenser is adapted to receive the salt vapor.

Embodiments of the invention provide systems and methods for heat transfer systems at temperatures in the range of 20 C to 800 C. The systems consist of heat pipes configured such that they fit inside conventional heat exchangers, and more effectively transfer or recover heat from hot fluids, and that operate without user intervention over long periods of time.

A system and method for thermal cracking of crude oil is provided. The system includes a plurality of communicatively coupled components configured to support thermal cracking of crude oil and performs a method including a continuous, industrial-sized thermal cracking process used to convert heavy crude oil or extra-heavy crude oil into lighter crude oil, using a liquid catalyst to prevent coke formation and promote alkylation reactions.

The disclosure provides a botanical processing module, comprising a housing, wherein the housing comprises a plurality of surfaces, wherein there is an internal cavity defined between the plurality of surfaces; a first inlet disposed on a top surface of the housing; a second inlet disposed on a first side surface of the housing, wherein the first side surface is orthogonal to the top surface; a first outlet disposed on the first side surface; a controller, wherein the controller comprises a processor; a memory; and a display, wherein the display is disposed on a second side surface of the housing, wherein the second side surface is orthogonal to both the top surface and the first side surface; a grinder; and a first heating chamber; wherein the grinder and the first heating chamber are disposed within the internal cavity of the housing, wherein the first heating chamber is coupled to the grinder.

The water desalination system using geothermal energy includes a plurality of heat transfer rods. Desalinated water flows into the injector and reaches the evaporation chamber, wherein the evaporation chamber receives heat geothermally via a plurality of heat transfer rods 18. Further, the heat transfer rods 18 heat the water in the evaporation chamber, which results in the formation of steam. The steam is carried to one or more storage tanks by means of one or more pipes. The steam generated from the evaporation chamber on reaching the storage tanks get condensed and water is formed.

A vaporizer includes a tank body, a porous member disposed in the vaporizer and heated, a supply tube configured to supply a liquid material to the porous member, and a gas discharge passage configured to discharge a source gas produced by vaporizing the liquid material to the outside. An outlet of the supply tube is disposed in contact with or in close proximity to the porous member. When the outlet is disposed in close proximity to the porous member, a separation distance between the outlet and the porous member is not greater than a distance from the outlet to a bottom of a droplet of the liquid material formed and suspended at the outlet by surface tension.

The State of California has been in severe drought conditions yet ironically it is surrounded by oceanwater. Existing desalination systems require expensive electrical power to produce clean potable water. This invention creates its own electrical power input, and even EXTRA ELECTRICAL POWER to supplement California's electrical power grid (part of this inventor's other U.S. patent application Ser. No. 16/598,965.

Desalination and Distillation are two concepts that now belong to public domain and are not owned by anyone. Oceanwater is boiled and salt is left behind, in the process producing clean potable water. Steam is cooled down using cooling coils similar to car radiator, using a blower fan and oceanwater sprinklers.

The present invention relates to a method for producing purified phosgene vapor, comprising the following steps: 1) providing a gas flow obtainable from the reaction of chlorine with carbon monoxide and comprising phosgene and carbon monoxide; 2) one-stage or multi-stage condensation of the gas flow and separation of non-condensable residue gases; 3) one-stage or multi-stage evaporation of the liquid phosgene obtained in step 2) and optional overheating of the produced phosgene vapour, wherein there is an energy integration between one or more of the condensation steps of step 2) and one or more of the evaporation steps in step 3) and the pressure in the last condensation step is between 0.2 and 6.0 bar higher than in the first evaporation step.