A method and system for balancing water content in a liquid mixture is described. The method includes using an direct column contact evaporator to reduce the water content in the liquid mixture. The liquid mixture is provided in the open column direct contact evaporator with relatively dry air. The dry air evaporates excess water from the liquid mixture to concentrate the liquid mixture while at the same time reducing the energy required for water evaporation elsewhere in the plant.

A device capable of stably obtaining gas of a sterilizer containing hydrogen peroxide for a long time is provided. A cleaning device that cleans a heating surface that gasifies a sterilizer of a gasifier for a sterilizer is provided, and after an operation for a fixed time period, the heating surface is cleaned.

A device capable of stably obtaining gas of a sterilizer containing hydrogen peroxide for a long time is provided. A cleaning device that cleans a heating surface that gasifies a sterilizer of a gasifier for a sterilizer is provided, and after an operation for a fixed time period, the heating surface is cleaned.

A system and method for concentrating wastewater with a heated gas is disclosed wherein a heated gas directed into a first wastewater heating chamber at a first velocity and a first wastewater stream is directed into the first wastewater heating chamber. A second wastewater heating chamber coupled to the first wastewater heating chamber and in fluid communication with the first wastewater heating chamber is disclosed. The wastewater streams and heated gas are propagated to optimize the water drop size within the heating chambers.

A system and method for concentrating wastewater with a heated gas is disclosed wherein a heated gas directed into a first wastewater heating chamber at a first velocity and a first wastewater stream is directed into the first wastewater heating chamber. A second wastewater heating chamber coupled to the first wastewater heating chamber and in fluid communication with the first wastewater heating chamber is disclosed. The wastewater streams and heated gas are propagated to optimize the water drop size within the heating chambers.

Provided is a process for separating an organic isocyanate prepared by reacting an organic amine with a stoichiometric excess of phosgene in the gas phase from the gaseous crude product obtained in the reaction, the process comprising the steps of (i) at least partially condensing the crude product stream containing at least the isocyanate, hydrogen chloride and unconverted phosgene by contacting with at least one liquid stream containing at least one quench liquid in a first separation apparatus to obtain a liquid stream containing at least some of the quench liquid and some of the isocyanate and a gas stream containing at least hydrogen chloride, evaporated quench liquid and phosgene, (ii) discharging the liquid stream obtained in step (i) via a first liquid outlet and of the gas stream obtained in (i) via a first gas conduit and (iii) at least partially condensing and/or absorbing the gas stream discharged in step (ii) through the first gas conduit, wherein that the at least partial condensation and/or absorption is effected in step (iii) by direct introduction of at least one cooling fluid, wherein the cooling fluid is introduced directly into the first gas conduit via at least one addition unit assigned to the first gas conduit.

An evaporation unit for evaporating liquid from a solution, comprising: a plurality of evaporation elements extending radially outwardly from a common central axis, the evaporation elements being configured for rotation about the central axis; and a liquid discharge system for distributing the liquid onto the evaporation elements to promote evaporation.

A method of separating a feed stream in a distillation tower. Vapor is permitted to rise upwardly from a distillation section of the distillation tower. A feed stream is introduced into a controlled freeze zone section of the distillation tower, the controlled freeze zone section being situated above the distillation section. The feed stream is released above a level of a liquid retained by a melt tray assembly in the controlled freeze zone section. Vapor from the distillation section is directed into the liquid retained by the melt tray assembly. A solid is formed from the feed stream in the controlled freeze zone section.

A water hydration system for disposing of the water content of production fluid generated by a hydrocarbon well. The production water is processed to remove particulate matter, and then to separate the water from crude oil. The water is heated and pressurized and passed through a nozzle to produce a spray which flashes into steam in a duct carrying fresh air. The water vapor hydrates the air that is forced through the duct by a high capacity fan which blows the hydrated air into the atmosphere.

The system and methods described are directed to a distillation system and method having an evaporator tank with a wall surrounding an interior evaporator tank area. A non-oxidizing gas line is disposed at least partially outside the evaporator tank in communication with the interior evaporator tank area, wherein the non-oxidizing gas line introduces a non-oxidizing gas into the interior evaporator tank; the interior evaporator tank area is generally at or above an ambient atmospheric pressure.