Abstract: The invention relates to a mechanical vapour compression (MVC) desalination arrangement having a low compression ratio, with latent-heat exchangers having a high latent-heat exchange coefficient, with a temperature gradient between primary vapour and secondary vapour of approximately 1° C. or less, a compression ratio of 1.11 or less, high vapour volume, low overheating and a low-temperature saline solution to be desalinated, which arrangement allows industrial desalination with less specific energy per unit of desalinated water and is coupled to 100% renewable off-grid energy sources.

Abstract: A method to condense and liquefy vapor by introducing the vapor into a heat exchanger and bringing same into contact with a cooling body in the heat exchanger, wherein a droplet condensation promoting agent is directly added to the vapor introduced into the heat exchanger or to the heat exchanger. A droplet condensation promoting effect due to the droplet condensation promoting agent can be sufficiently manifested and condensation efficiency by droplet condensation can be improved by way of directly adding the droplet condensation promoting agent such as a film forming amine or the like to the vapor introduced into the heat exchanger or to the heat exchanger.

Abstract: A gas compression system includes a system inlet to receive a gas stream containing a first component and a second component, a vapor system outlet to discharge the gas stream, and a plurality of compression stages coupled in series between the system inlet and the vapor system outlet. Each of the plurality of compression stages includes a compressor, a condenser coupled to the compressor, and a gravity-independent phase separator coupled to the condenser. The compressor is configured to receive the gas stream from either the system inlet or another of the plurality of compression stages and compress the gas stream. The condenser is configured to condense the second component from the gas stream. The gravity-independent phase separator is configured to remove the second component from the gas stream and discharge the gas stream to either the system outlet or another of the plurality of compression stages.

Abstract: The present invention relates to an energy saving method for separating an unreacted monomer, by which an unreacted monomer may be easily recovered from a mixture solution including an unreacted monomer, and a separation system which is capable of performing the method.

Abstract: Disclosed are a vapour-liquid filter mesh, a heat exchanger and an air conditioner. The vapour-liquid filter mesh includes a first area located in the middle and a second area located at the periphery of the first area, and the thickness of the second area is greater than the thickness of the first area.

Abstract: Methods and systems for conducting batch multi-effect distillation are disclosed. A multi-effect distillation system and one or more isolation devices are provided. A feed stream, consisting of water and a solute, is passed from a feed source into a brine side of the plurality of heat exchangers. The feed source is isolated from the plurality of heat exchangers by closing the one or more isolation devices. A first of the plurality of heat exchangers is heated by the heat source. A steam stream and a brine concentrate stream are produced in all but a last of the plurality of heat exchangers. A condensate stream from the steam stream is produced in all but the first of the plurality of heat exchangers. A warmed feed stream is produced in the last of the plurality of heat exchangers.

Abstract: The invention is a high-salt waste water air powered low temperature evaporating device and method of use. A tray is mounted on a lifting platform; an air inlet and a water inlet are on the tray. Air distributing pipes are arranged at the center of the nested column tubes (33). A groove (4) is installed at the top of the tray, and mounting points are accompanied by multiple nested column tubes (33). The nested column tubes (33) are connected with the air inlet. An atomizer is arranged inside the air distributing pipes; and the atomizer is connected with the water distributing pipes. Using air power evaporates concentrated waste water multiple times so that the salt in the wastewater reaches saturated concentration, and therefore, the wastewater temperature is reduced, salt is crystallized and separated out, liquid is continuously evaporated, and the wastewater can be completely treated.

Abstract: An apparatus for heating fluid and distilling fluid includes a main tank for containing fluid to be heated by a main gas heater, the main gas heater including a pilot light for heating the main tank, a condensing tank for passing fluid to the main tank, the condensing tank containing one or more heat conducting rods that allow heat to be conducted to the lower region of the condensing tank, an evaporator tank for vaporizing fluid received therein, the evaporator tank being heated by the pilot light, a condensing coil, disposed in the condensing tank, for exchanging heat between fluid vaporized by the evaporator tank and fluid in the condensing tank, a holding tank for receiving fluid from a main source, a delaying float bowl tank to receive fluid from the holding tank, the delaying float bowl tank including a first fluid flow regulator for regulating fluid flow to the evaporator tank according to an amount of fluid in the delaying float bowl tank, and a distillate tank for receiving condensed fluid from the c

Abstract: The present invention provides a rotary evaporator capable of accurately quantifying concentrated liquid and/or distillate. A distillation flask is improved into a structure having a liquid discharge opening formed at the bottom, and/or a spherical collecting flask is improved into a structure having a liquid release opening formed at the bottom. Concentrated liquid and/or distillate can be discharged without dismounting the distillation flask and/or the collecting flask. In addition, fine metering scale tubes and quantitative capacity increase units are disposed at the liquid discharge opening and/or the liquid release opening, there is a valve on the top and another valve on the bottom of each tube, so that the constant subtle changes of the amount of concentrated liquid and/or distillate can be observed, and an accurate amount of concentrated liquid and/or distillate can be discharged.

Abstract: A solar-powered system includes a support portion; and an evaporation portion having a pumping layer and a photothermal layer. The support portion pumps a fluid to the evaporation portion, the pumping layer evaporates the fluid based on solar power; and the photothermal layer is insulated from the pumping layer.

Abstract: A system for the removal of gaseous pollutants including smoke, exhaust and other gases that are released into the atmosphere, comprises means for enclosing the gaseous pollutants that are released into the atmosphere and for transporting them through tubing and ductwork. Means for filtering the gaseous pollutants through a filtration system and then mixing the gaseous pollutants exiting the filtration system with steam. Means for cooling the gaseous pollutants mixed with steam exiting the filtration system with a mist to convert the pollutants being cooled from a gaseous state to a liquid state, while concurrently disposing of the smoke, exhaust, liquid and solid particulates that are in the pollutants.

Abstract: Disclosed are polyurethane-based foams. The foams may have one or more vicrucidal/bactericidal agents. The foams may be used as filters that capture and/or inactivate viral particles, such as, virions associated with COVID-19. Also described are methods of making the foams and methods of using the foams.

Abstract: 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 chan

Abstract: A filter assembly that includes a filter housing with a housing interlocking feature, a filter cover with a filter cover interlocking feature, and a filter element with a filter element interlocking feature is disclosed. The filter element is positionable within the filter housing, and the filter cover is attachable to a top portion of at least one of the filter element and the filter housing. The housing interlocking feature, the filter cover interlocking feature, and the filter element interlocking feature are interlockable with each other and extend in a nonplanar configuration along at least one side of the filter element when the filter housing, the filter cover, and the filter element are assembled together.

Abstract: Extraction of anhydrous hydrogen fluoride from its aqueous solution is provided. A method provides hydrogen fluoride from aqueous solutions, including the reduction of water component of the aqueous solution at an elevated temperature into carbon oxide, carbon dioxide and hydrogen. The condensation and distillation of the obtained hydrogen fluoride and water vapor are characterized by the fact that the mixture of hydrogen fluoride and water is reduced at a temperature of 800 K and above, the molar ratio of carbon to water in the reducing agent is from 0.5 to 4, and using a reducing agent of the general formula CnHmOk, where k?0, m>0, and n>0, and the reducing agent may be saturated, unsaturated, aromatic hydrocarbons, oxygen-containing organic compounds, their isomers and their mixtures. The method makes it possible to extract hydrogen fluoride from its mixtures with water in any ratio and from azeotropic mixtures.

Abstract: The present description provides high working capacity adsorbents with low DBL bleed emission performance properties that allows the design of evaporative fuel emission control systems that are lower cost, simpler and more compact than those possible by prior art. Emission control canister systems comprising the adsorbent material demonstrate a relatively high gasoline working capacity, and low emissions.

Abstract: Disclosed are a desalination device and processes of desalination using the device. The device is directly ocean-situated and fully nature-powered with on intake, no brine production, and no electricity consumption. The device contains a heating unit, configured to receive a dry air stream and heat the dry air stream with one or more renewable energy sources to produce a heated air stream; a humidifier, configured to receive the heated air stream, evaporate at least portion of water present in the humidifier and humidify the heated air stream to produce a wet air stream, a cooling unit, configured to receive the wet stream and cool the wet air stream resulting in condensation of at least a portion of the moisture to produce fresh water and a dehumidified air stream; and a fresh water collection tank, configured to collect at least a portion of the fresh water.

Abstract: A process for separating distillate and waste from a water stream comprising: spraying the water stream together with compressed steam through one or more dual phase nozzles down into one or more vertical tubes contained in a shell and tube heat exchanger; evaporating water condensing the distillate; and ejecting the waste.

Abstract: A continuous feeding process and device for waste flexible polymer material; wherein the process continuously feeds waste flexible polymer material into a subsequent pyrolysis apparatus following compression, cutting and dispersion; the waste flexible polymer material is pre-treated during compression, cutting and dispersion to achieve continuous sealing feeding, while pyrolysis oil gas preheats and self-lubricates the device; the device used includes a feeding apparatus, a material dispersion apparatus and a screw feeder; the material is compressed, cut and dispersed in the feeding apparatus and the material dispersion apparatus, and then falls into the screw feeder, being preheated and thermally sealed by the pyrolysis oil-gas in the screw feeder; by using such a process, waste flexible polymer material from various sources may be continuously fed for pyrolysis, fully using the temperature of an oil-gas generated in a pyrolysis machine for preheating and device lubrication.

Abstract: A distillation and desalination system can include a refrigeration unit and a vacuum source positioned in the refrigeration unit. The vacuum source can include a first chamber defining a first chamber volume, a second chamber defining a second chamber volume, a flexible diaphragm dividing the first chamber and the second chamber; and a check valve permitting gas transport into and out of the first chamber, the check valve comprising an inlet and an outlet. The system can also include a distillation unit having a distillation chamber, a saline liquid in the distillation chamber, and a headspace above the saline liquid, the headspace comprising a gas. The inlet of the check valve can be fluidically coupled to the headspace of the distillation unit.