摘要:
The invention discloses a condenser for a bioreactor exhaust, comprising: an inlet (1) adapted to be fluidically connected to a bioreactor exhaust port (2), a cooling chamber (3; 103) fluidically connected to the inlet and via a filter device (4) to an outlet (5), a cooling conduit (6; 106) in contact with the cooling chamber, a heating conduit (7) in contact with the filter device and a vortex tube (8) arranged to convey a cold gas stream through the cooling conduit and to convey a hot gas stream through the heating conduit.
摘要:
Die vorliegende Erfindung betrifft eine Anlage zum Entalkoholisieren von alkoholhaltigen Getränken, umfassend eine Rektifikationskolonne (26) mit wenigstens einem Zulauf für das alkoholhaltige Getränk, einem Sumpf und einem Kopf, wobei die Rektifikationskolonne (26) derart betreibbar ist, dass aus dem Sumpf entalkoholisiertes Getränk und aus dem Kopf Brüden entnehmbar sind, wenigstens einen Verdampfer (27), welcher dazu eingerichtet ist, die Rektifikationskolonne (26) mit Dampf zu versorgen; und eine Kondensatoranordnung (30) zum wenigstens teilweisen Kondensieren des aus dem Kopf der Rektifikationskolonne (26) entnommenen Brüden. Hierbei umfasst die Anlage ferner eine Wärmepumpe (70), mittels welcher sowohl der Verdampfer (27) als auch die Kondensatoranordnung (30) betreibbar sind. Des Weiteren betrifft die Erfindung ein Verfahren zum Entalkoholisieren von alkoholhaltigen Getränken in einer Rektifikationskolonne.
摘要:
The present invention relates to vapour-solids separations, and in particular provides a process for the separation of a stream comprising vapour and a stream comprising solids from a stream comprising vapour and solids using a separation vessel, said separation vessel having: a. a first inlet for the stream to be separated, b. a liquid outlet, c. a vapour outlet, d. a demister located on the vapour outlet, and e. a second inlet by which liquid can be passed to the demister said process comprising (i) passing the stream comprising vapour and solids through the first inlet and in to the separation vessel, (ii) recovering from the vapour outlet a vapour stream which comprises vapour from the stream comprising vapour and solids and which vapour stream has passed through the demister in the separation vessel, (iii) passing to the separation vessel, via the second inlet, a first liquid stream which contacts the vapour stream in the demister, and (iv) recovering from the liquid outlet a second liquid stream which comprising the solids from the stream comprising vapour and solids, and liquid from the first liquid stream.
摘要:
A filter device (60) for a resin vessel is described. The filter device (60) comprises a housing (61) having a first end (62) and a second end (64). When seen from the first end (62) towards the second end (64), the filter device (60) comprises: a first demister layer (66) having a first end (68) and a second end (70) and having a first thickness, a second layer (72) having a first end (74) and a second end (76) and having a second thickness and comprising silica, and a third layer (78) having a first end (80) and a second end (82) and having a third thickness and comprising activated carbon, the layers (66, 72, 78) of the filter device being arranged within the housing (61). The filter device (60) further comprises: an inlet (84) for receiving a gaseous fluid provided at the first end (62) of the housing (61), and an outlet (86) for emitting the gaseous fluid after having passed the layers (66, 72, 78) of the filter device (60), the outlet (86) being provided at the second end (64) of the housing (60).
摘要:
The invention relates to a method for producing a polyalkenyl amine in which the solvent used for the production is exchanged for a different solvent.
摘要:
An apparatus and method for fluid distillation in general, and in particular, of water, adapted for consumer or home use, but capable of being made and operated so that it is suitable for separating solvents and solutes and other industrial use. The apparatus includes a housing (12) having divider structure to form one or more compartments (26) for receiving water to be distilled. The divider structure also presents a fluid passage for receiving water vapor which is formed when the upper portion of the water in the housing is boiled by a heater. An aerator (34) is provided in the housing below the heater (50) and in a location within the water compartment. The aerator (34) operates to direct air under a slight pressure into the water so that air bubbles can be generated in the water. The air bubbles will rise and break the surface of the water as the upper part of the water is being boiled by the heater. This causes a vapor pressure to be generated in the space above the water level and water vapor is then caused to move through the fluid passage (24) downwardly to a lower chamber in which the water vapor is collected as a condensate. As the water vapor moves downwardly in the fluid passage (24), it moves in heat exchange relationship to the water in the compartment of the housing.
摘要:
The invention relates to a method for processing a liquid medium, wherein the medium to be processed is conducted through a liquid circuit (48) and the medium to be processed is heated up in the liquid circuit (48) with the aid of a heat exchanger (62). In order to achieve economical processing of the liquid medium, a liquid-vapor separation process is carried out in a separating device (32), and a liquid obtained in the liquid-vapor separation process is conducted into the heat exchanger (62) as a heating medium.
摘要:
An off gas purification system provides superior results to other systems for removing volatile organic compounds from off gas, especially off gas from soil, groundwater, industrial processes, pipelines and storage tanks. Off gas is extracted, followed by compression and condensation. Compression and condensation produce an off gas that must be further treated to produce pollutant-free exhaust. A separation device cleans the influent gas/air by separating residual chemical vapor from the gas stream and returning that chemical vapor to the compression and condensation step. After removal of all detectable volatile organic compounds, the air stream may be further separated into segregated gases, and heated gas is used to thermally enhance the desorption or degradation of volatile organic compounds from the off gas source or a separation device. Methods of accomplishing the same are similarly provided, including unique business methods for conforming extraction and processing plans with current environmental regulations and compliance impact generation based on an evolved knowledge base.
摘要:
In cooling plants which work with water as both primary and secondary coolant, it is customary for use to be made of both an evaporator and a condenser which must be supplied wi5th water in the form of e.g. a spray for achieving an effective heat exchange, and out of regard for the effectiveness it is necessary for a continuous deaeration of the water to be carried out, which is effected by the sucking of air direct from the condenser, possibly supplemented with an external NCG condenser or by leading the supply water through a pre-deaerator under vacuum. With the invention it has been found possible to configure both the evaporator and the condenser with associated deaeration/pre-deaeration units in a fully integrated manner, namely by mounting a pair of sieve plates in a vacuum container for the dividing of the container into an upper supply- and distribution chamber, a centremost pre-deaeration chamber (one or more), and a bottom chamber in the form of an evaporator- and a condenser chamber respectively. From the sieve plates, the water will flow down in many thin jets, which in the deaerator chamber can be pre-deaerated by a moderate suction pressure for independent air separation, while the thin jets introduced into the bottom chamber can create effective heat exchange therein. The exchange of heat can be made additionally effective by use of a jet-breaking insert in the form of e.g. a net in the bottom chamber. The sucking of air from the condenser and from the pre-deaeration stages is arranged with stepwise air concentration units and pumps for minimizing the necessary vacuum pump capacity and energy consumption.