Systems and methods for the removal of scale in humidification-dehumidification desalination apparatuses are generally described.

Processes and plants for the production of purified urea solution are described. In a described urea production process, urea is produced in a synthesis section without a high pressure stripper and the urea solution is subjected to purification after the recovery section, to give purified urea solution and off-gas. The purification comprises e.g. steam stripping.

A system (100) for producing aqueous sulphuric acid. The system (100) comprises a first heat exchanger (410) configured to cool water and/or aqueous sulphuric for producing cooled water and/or cooled aqueous sulphuric acid; a pre-cooling unit (200) configured to pre-cool some gas containing sulphur trioxide, the pre-cooling unit (200) comprising an inlet or inlets (212, 214) for receiving [i] the gas containing sulphur trioxide and [ii] the cooled water and/or the cooled aqueous sulphuric acid, an outlet (216) for letting out aqueous sulphuric acid and the gas containing sulphur trioxide, and a first nozzle (220) for spraying the cooled water and/or the cooled aqueous sulphuric acid onto the gas containing sulphur trioxide to cool the gas containing sulphur trioxide. The system further comprises a condensation tower (300) comprising a first inlet (302) for receiving the cooled gas containing sulphur trioxide and aqueous sulphuric acid from the pre-cooling unit (200) and means (320) for circulating the aqueous sulphuric acid within the

A method for continuously removing water vapor from a carrier gas is disclosed. This method includes, first, causing direct contact of the carrier gas with a liquid mixture in a separation chamber, the carrier gas condensing at a lower temperature than the water vapor. A combination of chemical effects cause the water vapor to condense, complex, or both condense and complex with the liquid mixture. The liquid mixture is chosen from the group consisting of: first, a combination of components that can be maintained in a liquid phase at a temperature below the water vapor's condensation point, whereby the water vapor condenses into the liquid mixture; second, a combination of components where at least one component forms a chemical complex with the water vapor and thereby extracts at least a portion of the water vapor from the carrier gas; and third, a combination of components that can both be maintained in a liquid phase at a temperature below the water vapor's condensation point, and wherein at least one component forms a chemical complex with the water vapor and thereby extracts at least a portion of the water vapor from the carrier gas. The liquid mixture is then reconstituted after passing through the separation chamber by a chemical separation process chosen to remove an equivalent amount of the water vapor from the liquid mixture as was removed from the carrier gas. The reconstituted liquid mixture is restored to temperature and pressure through heat exchange, compression, and expansion, as necessary, in preparation for recycling back to the separation chamber. The liquid mixture is then returned to the separation chamber. In this manner, the carrier gas leaving the exchanger has between 1% and 100% of the water vapor removed.

A method for recovering organic carbonates in an electrolytic solution of a waste lithium ion battery is provided. The organic carbonates include a first carbonate and a second carbonate having a higher melting point and a higher boiling point than the first carbonate. The method includes performing a temperature adjustment process in which an internal temperature of a drier in which the waste lithium ion battery is accommodated is kept in a first temperature range, an internal temperature of a pipe extending to below the drier is kept in a second temperature range, and an internal temperature of a condenser connected to the drier via the pipe is kept in a third temperature range, and performing a recovery process of reducing internal pressures of the drier, the pipe, and the condenser from a normal pressure to a first pressure and recovering the first carbonate in the condenser.

The small-sized water treatment equipment providing high water treatment efficiency without using multi-stage structure in the water treatment equipment for obtaining fresh water from raw water, including sea water.

The water treatment equipment 10 comprises the evaporation parts 11 and 12, the condenser part 13 and the heat exchanger 24, and the raw water, including sea water, being introduced within the equipment circulates between the evaporation parts 11 and 12 and the heat exchanger 24 via circulating the circulation paths 40a to 40d. Further, circulating water circulates between the condenser part 13 and the heat exchanger 24 via circulating the circulating water circulation paths 41a to 41c, being vaporized at the evaporation parts 11 and 12 and cause vapor-liquid contact in the condenser part 13 with the steam that has circulated the air flow channels 42a to 42c. The circulating water that passed the condenser part 13 and the raw water that passed the evaporation parts 11 and 12 exchange heat at the heat exchanger 24.

The duty of internal heat exchange can be flexibly adjusted without impairing energy saving performance of a HIDiC. A method of adjusting the duty of heat exchange in a heat exchange structure of a HIDiC includes totally condensing a portion of the vapor fed to a heat exchange structure in a heat exchange structure; and providing a liquid control valve downstream of the heat exchange structure on the first line, without providing a control valve on a vapor-flowing part of first and second lines of the HIDiC, and adjusting a flow rate of a portion of the compressor outlet vapor flowing into the heat exchange structure by using the control valve, while compensating for a pressure loss needed for the control valve by using a liquid head of a condensate, and/or by using pressurization by a pump.

Provided is a catalyst article for simultaneously remediating the nitrogen oxides (NOx), particulate matter, and gaseous hydrocarbons present in diesel engine exhaust streams. The catalyst article has a soot filter coated with a material effective in the Selective Catalytic Reduction (SCR) of NOx by a reductant, e.g., ammonia.

An operations unit, comprising: a first chamber; a second chamber; a conduit extending through the first chamber and into the second chamber, the conduit being at least partially enclosed by a conduit jacket that defines an outer diameter, the conduit placing the second chamber into fluid communication with an environment exterior to the chamber, the second chamber comprising a wall facing the conduit jacket, and the second chamber being rotatable relative to the first chamber; a seal defining a boundary between the first chamber and the second chamber, the seal extending radially from the wall of the second chamber toward the conduit jacket, the seal comprising a flange, the flange defining an inner diameter, (a) the seal comprising a layered portion that comprises a plurality of ring-shaped portions, or (b) the seal comprising a brush that rotatably abuts the conduit jacket.

Embodiments relate to systems and methods directed towards arrangements of a preheater, a heat exchanger, a plasma recovery system, and at least one processing stage configured to use steam output of a calciner for heating incoming wastewater that is being processed.