A cold trap has multiple interior spaces formed within one unit such that a vacuum pump pulls only dry air and distillate substantially fully or fully condenses and drops out of the bottom of the device. Laminar flow through a side portal is converted into turbulent flow in a cooling region around a conical cold glass or other inert protrusion. The only other portal of the cooling region is a bottom portal such that though there is vacuum suction, vapors only exit through the bottom portal after condensing and falling through an outer section while dry air is pulled upwards to an upper vacuum portal.

Device for heating a substrate includes a process chamber having a first and a second sealable opening for a substrate to pass through, a first inlet for receiving a process gas and a first outlet for discharging an off-gas; an evaporator for evaporating the material, which evaporator device is connected to the chamber for supplying the process gas; a first condensation device connected to the chamber for receiving the off-gas and condensing the material in the vapour phase in the off-gas to form a solid phase and a second condensation device for condensing part of the material in vapour phase in the off-gas to form a liquid phase, which second condensation device connects the first condensation device to the discharge duct and a connecting duct between the evaporator device and the second condensation device for transporting material in the liquid phase between the second condensation device and the evaporator.

The present disclosure is related to systems and methods for the biological processing of hydrocarbon-containing substances. In particular embodiments, the systems and methods herein relate to pre-digestion of hydrocarbon containing substances and further processing of the same to produce hydrocarbon fuels, fertilizer, and other products.

A method for cryogenic cooling without fouling is disclosed. The method comprises providing a first cryogenic liquid saturated with a dissolved gas; expanding the first cryogenic liquid into a separation vessel, separating into a vapor, a second cryogenic liquid, and a first solid; drawing the vapor into a heat exchanger and the second cryogenic liquid and the first solid out of the separation vessel; cooling the vapor against a coolant through the heat exchanger, causing the vapor to form a third cryogenic liquid and a second solid, the second solid dissolving in the third cryogenic liquid; and combining the second cryogenic liquid and the first solid with the third cryogenic liquid, producing a final cooled slurry. In this manner, the cryogenic cooling is accomplished without fouling.

A method is disclosed for recovering a useful gas from a gas mixture including a useful gas and at least one secondary gas. The gas mixture is first compressed and transferred into a pressure vessel where cooling occurs. Then, from the pressure vessel, a secondary-gas containing gas phase is removed and condensed useful gas is transferred into a purification vessel. In the purification vessel, the condensed useful gas is then purified. A plant is disclosed for recovering a useful gas from a gas mixture. Finally, the use of a plant for carrying out a method for recovering a useful gas from a gas mixture is disclosed.

An atmospheric water generation system, including a casing into which an air treatment unit and a chiller unit are located, the air treatment unit being provided with a first air inlet for ambient air and a first air outlet, the chiller unit being provided with a second air inlet and a second air outlet, wherein a respectively closing member is directly associated to each first and second air inlet and outlet. The system thus can additionally be used as an air conditioning unit, when the cooled and demoistured air from the air treatment unit is directed to a closed work space. The system may additionally include a water treatment unit and a power generating unit for stand alone purposes.

A method of removing inert gas dissolved in liquid ammonia involves evaporating, compressing, and then condensing the liquid ammonia together with the inert gas dissolved therein. Thereby, a product stream of warm liquid ammonia that has been freed of the inert gas is obtained, which is under elevated pressure relative to standard pressure and hence suitable for immediate use in methods in which pure liquid pressurized ammonia is required. If, by contrast, the ammonia is cooled first, for example, below the boiling temperature for ammonia and expanded to standard pressure to store it in tanks as liquid ammonia at low temperatures, it is necessary first to reheat and compress it for further processing operations. Thus the disclosed methods lead to significant energy savings.

A horizontal sulfur condenser may include an exterior casing with a plurality of condenser tubes arranged longitudinally within the casing, a liquid sulfur reservoir at a longitudinal end within the exterior casing, and an internal baffle that protrudes into the liquid sulfur reservoir from the surface. The lowest of the plurality of condenser tubes is parallel to a wall of the exterior casing. A Claus process gas inlet is proximate a first end of the plurality of condenser tubes, which are arranged horizontally but are positioned vertically above the sulfur reservoir. A liquid sulfur outlet is located at the liquid sulfur surface. The baffle creates multiple chambers above the sulfur reservoir, such as a first chamber defined by the exterior casing and the baffle to receive condensed Claus sulfur in the liquid reservoir, and a second chamber defined by the exterior casing and the baffle to receive degassed liquid sulfur.

Disclosed herein is a system and method for condensing moisture in a moist gas stream entering a bioreactor or leaving a bioreactor, the system comprising: a condenser container capable of holding a fluid, the condenser container comprising: an outer wall surface and an inner wall surface, the inner wall surface defining an interior chamber for holding the fluid; and a first fitment attached to the outer wall surface of the condenser container, the first fitment forming a first port configured to allow the moist gas stream to flow through the first port and into the interior chamber; a second fitment attached to the outer wall surface of the condenser container, the second fitment forming a second port configured to allow a dried gas to flow from the interior chamber and out of the second port; and a cooling device in contact with at least one portion of the outer wall surface of the condenser container and arranged to cool the at least one portion of the outer wall surface of the condenser container, thereby to condense moisture in the moist gas stream and forming a dry gas stream for entering or leaving the bioreactor.

Vapor flow-diverting devices that re-direct upwardly flowing vapor, for example, in a downward direction across condenser tubes disposed in the upper or top section of a vapor-liquid contacting apparatus, are described. These devices are particularly beneficial in tubular condensers within distillation columns and may be used in combination with other associated equipment (e.g., a deflector plate and divider plate) as well as in combination with the tube surface enhancements to improve the heat transfer coefficient.