The invention relates to an apparatus for the conditioning of gases, in particular of sealing gas, comprising a separator unit for separating liquids and/or particles from the gas flowing through the apparatus, and comprising a collecting container for the trapped substances.
Apparatuses of this kind are prior art. One area of application of such apparatuses is the conditioning of sealing gas. When handling corrosive process gases, for example, during pumping using turbo compressors, there is the known risk of sensitive parts of the pump, bearing points and/or sealing systems being attacked due to solid particles along with moisture present in the associated process gas. To counter this risk, sensitive parts, for example, the bearing points, must be protected by sealing gas in the form of a continuous flow of inert gas, the inert gas flowing over the parts of the system to be protected. An appropriate inert gas may be dry nitrogen. During operation, the pressure of the sealing gas should be higher (for example, approximately 3 bar) than the process gas pressure, so that no process gas is able to pass into the atmosphere. In view of the usually high pressure of the process gas, frequently greater than 100 bar, the gas conditioning apparatus must be designed up to a high pressure level.
Based on this prior art, the stated object of the invention is to provide an apparatus for the conditioning of gases, which is low-maintenance and, therefore, cost-effective to operate, and which is distinguished by an efficient separation effect.
The object is achieved according to the invention by an apparatus, which includes the features of patent claim 1 in its entirety.
Accordingly, an essential particular feature of the invention is that the separator unit includes a cyclone separator. By using a cyclone separator, a largely maintenance-free operation of the apparatus with highly efficient separation is feasible, making the apparatus cost-effective and efficient to operate.
According to another aspect of the invention, the stated object is achieved by an apparatus which includes the features of patent claim 2 in its entirety.
Accordingly, the invention is distinguished by the fact that the separator unit is mounted on the collecting container as a discrete, replaceable unit through which gas is able to flow. Adaptation to individual process conditions, such as type of gas, type of stresses caused by moisture and solid particles, by flow-through rates and the like, requires that only the separator unit be changed, while the collecting container together with the auxiliary equipment normally associated with it may remain in place. In view of the high pressure level of, for example, greater than 100 bar, and the corresponding complex, pressure-resistant construction, the potential for using the same collecting container with associated equipment, such as fittings and the like, under changing operating conditions is of great economic significance.
The separator unit may be advantageously mounted on the top of the collecting container and may be connected to the latter via an inlet opening of the collecting container.
With respect to the cyclone separator, it is possible to advantageously arrange it so that the former includes a cyclone housing, on which an inflow opening is disposed such that the gas flow within the housing forms a swirl flow about the vertical axis thereof, an outflow unit having an outflow channel extending upward coaxially relative to the vertical axis being provided on the cyclone housing.
For an outflow connection situated on the side of the cyclone housing, it is possible to alternatively configure the outflow unit in such a way that the outflow channel includes a section, which is connected to its initial vertical section and which extends horizontally to the inflow connection located on the side.
Thus, apparatuses adapted to different process conditions, in each case with an identical collecting container, may be implemented in the form of a modular system, by appropriately replacing the cyclone housing on the collecting container and/or, if needed, by equipping the cyclone housing with an outflow unit, which is designed for an outflow connection situated on the top, or for an outflow connection located on the side.
In particularly advantageous exemplary embodiments, the apparatus includes a gas cooler in the flow path of the gas flowing toward the separator unit. This opens up the possibility during operation of the apparatus of cooling the particular gas to a temperature below the dew point, for example, to a temperature of 10° K below the dew point, in order to form condensate from the vaporous phase for separation with the aid of the cyclone.
Preferably, a controllable outlet device for trapped fluid is provided at the bottom of the collecting container. In this case, it is possible to arrange for the outlet device to be manually controllable, for example, by means of a needle valve or ball cock provided at the particular outlet connection.
In advantageous exemplary embodiments, a sensor device which detects the fill level of trapped fluid may be attached to the collecting container. Such exemplary embodiments offer the possibility of providing an outlet device controllable in response to a signal of the sensor device, so that the system may be designed for automatic operation over longer operating periods.
Instead of a manually controllable outlet device or an outlet device or an outlet device controllable by a signal of the sensor device, an outlet device may also be provided for an automatic operation, which is controllable by a float situated in the collecting container.
The invention is described in detail below with reference to exemplary embodiments depicted in the drawing, in which:
In
As is most clearly seen in
Apart from the connections visible in
As shown in
As shown in
The exemplary embodiment of
In the two exemplary embodiments of
With the invention, a kind of modular system may be implemented by using different cyclone sizes and cyclone designs in conjunction with a collecting container 1 that has the same design with associated components, whereby further adaptations may be made by variously designing the outflow unit 45 for the outflow connection 9 located above or the lateral outflow connection 9, and/or different plugs 43 may be used for desired shapes of the acceleration cone 39.
As shown in
Number | Date | Country | Kind |
---|---|---|---|
10 2012 012 727.8 | Jun 2012 | DE | national |
Filing Document | Filing Date | Country | Kind |
---|---|---|---|
PCT/EP2013/001019 | 4/5/2013 | WO | 00 |