1. Field of the Invention
The invention relates to a receiver for a refrigerant for a refrigerant circuit, in particular of a motor vehicle, according to the preamble of claim 1, as well as to a capacitor with such a receiver.
2. Description of the Background Art
Receivers for a refrigerant of a refrigerant circuit are known in the art. These receivers stockpile the refrigerant to have sufficient refrigerant available in the refrigerant circuit even with operational fluctuations of the filling volume.
Further, a drying agent is often provided in the receiver in order to dry the refrigerant and to filter out moisture from the refrigerant.
In the refrigerant circuit, the receiver is often arranged after the capacitor or in the fluid stream between a condensation zone and a sub-cooling zone of the capacitor. The refrigerant hereby flows from the capacitor or from the condensation zone of the capacitor into the receiver where the refrigerant is separated into a gaseous phase and a liquid phase. The gaseous phase collects above the liquid phase in the receiver and the liquid phase can be discharged out of the receiver from below the gaseous phase.
If gaseous refrigerant is also channeled from the receiver into the subsequent sub-cooling zone, this gaseous refrigerant must first condense in the sub-cooling zone so that the further lowering of the refrigerant temperature for the gaseous portion cannot take place until the gaseous portion is condensed. This reduces the effectiveness of the sub-cooling zone since a part of its effectiveness does not cause the lowering of the temperature of the refrigerant, but only its condensation.
This ultimately results in that the maximum sub-cool temperature is not reached, and the effectiveness of the subsequent evaporator is thus not optimal.
The filling level of the receiver with refrigerant depends on the load condition of the refrigerant circuit but also on the filling volume and any possible leakages. In the process, refrigerant is channeled into the subsequent sub-cooling zone under any operating condition, i.e. at any filling level of the refrigerant in the receiver.
It is therefore an object of the invention to provide a receiver in which the gaseous portion in the liquid refrigerant flowing from the receiver is minimized over wide operating ranges or at different filling levels. The object is also to provide a capacitor with such a receiver.
An embodiment of the invention provides a receiver with a receiver housing having a fluid-receiving chamber, with a fluid inlet and a fluid outlet, wherein in the fluid-receiving chamber a drier is provided. An inlet channel featuring a channel outlet in the fluid-receiving chamber protrudes into the fluid-receiving chamber. The channel outlet allows fluid from the fluid inlet as inlet channel to pass into the fluid-receiving chamber, wherein the inlet channel is shaped in such a way that the fluid flowing out of the channel outlet flows in a lateral direction at a distance from the central axis of the receiver. This ensures that the fluid flows into the receiver on a circular or spiral path and that consequently a good separation of gaseous and liquid refrigerant in the fluid-receiving chamber of the receiver is achieved. As a result, the gaseous portion is reduced or avoided during the outflow of fluid from the receiver.
According to an embodiment of the invention, it is expedient when above the channel outlet there can be an unobstructed volume of at least 50% of the gross volume of the receiver in this section, and which extends over a height of, for example, at least 50% of the total internal height of the receiver.
It is hereby advantageous if a drier such as drying granulate is positioned below the channel outlet, on a side facing away from the unobstructed volume.
It is also useful when a drier such as drying granulate is positioned at an upper end of the receiver.
It is also advantageous if the receiver volume features an essentially constant cross-sectional area.
A cross section of the receiver can have a round shape.
Furthermore, in an embodiment of the invention, the receiver housing can have a round cross section with a cylindrical wall. This ensures that the fluid flowing from the channel outlet is forced in a circular flow towards the cylindrical wall of the receiver housing, allowing the gas portion to better rise and separate from the liquid portion.
The inlet channel can have at its channel outlet, an outlet port that is twisted by about 90° to a longitudinal axis of the channel. This allows the outflowing fluid stream to emerge approximately at a right angle to the longitudinal axis of the channel. This allows the fluid to essentially flow in a horizontal plane and to be forced onto a spiral path in order to lengthen the path of the fluid so that the phase separation is improved.
The channel outlet can be shaped as a pipe bend. This allows for a simple deflection of the fluid.
The channel outlet can be designed as an obliquely cut pipe end in which the long protruding pipe wall side is folded towards the short pipe wall side. Because the long protruding pipe wall side is bent towards the short pipe side wall by about 90°, an advantageous structure is achieved which corresponds to a simple deflection of about 90°. This structure is achieved by the oblique cutting of the pipe and the subsequent folding of a pipe wall side.
The drier can be arranged between two fluid-permeable retaining discs, wherein the inlet channel passes through at least one of the retaining discs, advantageously through both retaining discs. This way, the drier can be arranged between the two retaining discs, wherein the inlet channel penetrates the retaining discs. This ensures that the fluid does not directly traverse the drier on its way to the fluid-receiving chamber, but instead is separately channeled from the inlet channel through the drier. On the way back from the fluid-receiving chamber to the fluid outlet, however, the fluid must flow through the drier, i.e. through the retaining discs and the drying granulate arranged in between. Thus, the drier is only perfused once from entrance to exit of the fluid-receiving chamber.
The drier can be arranged between a base wall or a top wall and a fluid-permeable retaining disc. The drier may be located at the top or base area of the fluid-receiving chamber so that it is arranged in a space-saving and cost-effective manner with only one retaining disc.
The one retaining disc can be penetrated by the inlet channel. This is particularly the case when the drier is arranged at the lower portion of the receiver.
The inlet channel can be connected to a fluid deflector which deflects the flow of fluid from the fluid-receiving chamber to the fluid outlet. The direct route to the fluid outlet is thereby obstructed, resulting in a deflection of the fluid to extend the path for the fluid and promoting phase separation.
The fluid deflector can be a wall which is aligned essentially perpendicular to the longitudinal direction of the inlet channel.
Thus, a simple and inexpensive type of obstruction and deflection are obtained. The wall can be formed as a flat disc with an opening for the inlet channel to pass through.
A gap can be provided between the wall as fluid deflector and the wall of the receiver housing for the passing through of the fluid to the fluid outlet. Thus, a selectively dimensioned passage can be created without the need for separate components.
A filter can be arranged between the fluid deflector and the fluid outlet. This allows the fluid deflector to also serve as a filter support so that there is no need for a separate retainer. The retainer can be integrated into the fluid deflector.
The filter can cover the fluid outlet with one of its side surfaces and is covered by the fluid deflector on one of the opposite side surfaces. Thus, a defined arrangement and perfusion of the filter is attained. The mounting takes place between the edge area of the fluid outlet and the fluid deflector whereas the inflow towards the filter occurs laterally from the side.
The retaining disc can be a perforated plastic or sheet-metal disc. This enables the disc to be economically produced by injection molding or stamping.
The channel outlet can be designed as a pipe socket with an adapter piece, particularly of plastic, that is attached or inserted.
The fluid inlet and/or the fluid outlet can be arranged on a base plate of the receiver.
An embodiment relates to a capacitor for a refrigeration circuit, in particular of a motor vehicle, with a block having first and second fluid channels, wherein a refrigerant flows through the first fluid channels and a coolant flows through the second fluid channels, and wherein the first fluid channels are divided into a condensation zone for condensing the refrigerant and into a sub-cooling zone for the sub-cooling of the liquid refrigerant, wherein the receiver is arranged in the fluid stream between the condensation zone and the sub-cooling zone or after the sub-cooling zone.
Further scope of applicability of the present invention will become apparent from the detailed description given hereinafter. However, it should be understood that the detailed description and specific examples, while indicating preferred embodiments of the invention, are given by way of illustration only, since various changes and modifications within the spirit and scope of the invention will become apparent to those skilled in the art from this detailed description.
The present invention will become more fully understood from the detailed description given hereinbelow and the accompanying drawings which are given by way of illustration only, and thus, are not limitive of the present invention, and wherein:
In the base 4, a fluid inlet 6 and a fluid outlet 7 are provided. The fluid inlet 6 represents a hole through the base 4, as does the fluid outlet 7. A riser pipe 8 is arranged at the inside of the fluid inlet 6 which communicates with the fluid inlet 6 and essentially extends through the entire receiver in a vertical direction. If a refrigerant 9 flows through the fluid inlet 6, it passes through the riser pipe 8 vertically upwards and flows into the fluid-receiving chamber at the upper end of the riser pipe 8. There, the refrigerant essentially drops and reaches the fluid outlet 7 after flowing through the drier 10. The drier 10 is positioned approximately in the center of the receiver housing 2, wherein a portion of the drying granulate 11 is held between two perforated discs. The drying granulate is thus held on both sides of a perforated disc 12, 13, spaced at a distance from one another. The refrigerant 9 which flows out at the upper end of the riser tube 8, passes through the drier by flowing through the upper perforated disc and flowing past the drying granulate. It then flows through the lower perforated disc.
The fluid inlet 26 and fluid outlet 27 form openings or holes in the base 23 and serve for fluid communication between an external connection and the fluid-receiving chamber 25. In the interior of the fluid-receiving chamber 25, an inlet port 28 is provided which is fluidly connected to the fluid inlet 26 and which protrudes into the fluid-receiving chamber 25. The fluid inflowing through the fluid inlet 26, such as refrigerant 29, passes through the inlet channel 28 and exits from the channel outlet 30 of the inlet channel 28. The channel inlet 31 may coincide with the fluid inlet 26 or it may join the fluid inlet roughly where the inlet channel 28 starts at the base 23. Advantageously, the inlet channel 28 is a pipe which is inserted into the base 23 or is attached to the base 23. For this purpose, the pipe which forms the inlet channel 28 can be inserted in an opening of the base 23 or can be attached to or at an intake.
The inlet channel 28 is shaped such at its channel outlet 30 that, in interaction with the wall 22 of the receiver housing 21, it causes the fluid flowing out of the channel outlet 30 to assume a spiral-shaped flow inside the fluid-receiving chamber. For this purpose, the inlet channel 28 features at its channel outlet 30 an outlet port which is twisted about 90° to a longitudinal axis 32. This causes the outflowing fluid stream to leave the channel outlet 30 at about a right angle to the longitudinal axis of the channel 32. Spiral-shaped can be, for example, an arched or circular flow, or a flow moving roughly along a circular path, which can also be designed with a velocity component in the vertical position so that the fluid can move upwards or downwards from an inflow plane.
In further embodiments, the angle of 90° to the longitudinal axis of the channel can in this respect take on deviating values, for example between 45° and 135°, so that the flow of the fluid is channeled from the channel outlet 30 towards the cylindrical wall 22, while at the same time, the fluid stream also features a velocity component vertically upwards or downwards.
The effluent from the fluid outlet 27 encounters the cylindrical wall 22 with a velocity component and is deflected there to a circular arc or onto a spiral path.
With the inlet channel 28, a fluid deflector 33 is connected such that the fluid deflector 33 is designed as a specifically horizontal, for example, wall. The inlet channel 28 hereby penetrates the fluid deflector 33 so that a fluid flowing out of the channel outlet 30 cannot directly flow to the fluid outlet 27, but instead is deflected by this fluid deflector 33. The fluid deflector 33 is, for example, designed as a flat plate which is either formed together with the inlet channel 28 or connected to and supported by the inlet channel 28, wherein the inlet channel 28 can pass as a pipe through an opening of the fluid deflector 33. A gap 34 may remain between the edge of the fluid deflector 33 and the wall 22 through which the fluid 29 passes before it reaches the fluid outlet 27.
Between the fluid deflector 33 and the fluid outlet 27, a filter 35 which rests on the fluid outlet and is covered by the fluid deflector 33 can optionally be arranged. This causes a lateral inflow of the fluid 29 into the filter 35 so that the fluid in the filter 35 is essentially deflected by 90° before it arrives at the fluid outlet 27.
In the embodiment of
The drier 59 is arranged between two retaining discs 60, 61 which are penetrated by the tubular inlet channel 54. The fluid flows above the upper retaining disc 51 from the inlet channel 54 into the fluid-receiving chamber 56 and enters the drier through the upper retaining disc 61, a fluid-permeable retaining disc. There, it flows around the arranged drying granulate and then flows through the lower retaining disc 60 towards the fluid outlet 53.
Individual characteristics of different embodiments are generally combined with one another without loss of generality and without special mention.
The invention being thus described, it will be obvious that the same may be varied in many ways. Such variations are not to be regarded as a departure from the spirit and scope of the invention, and all such modifications as would be obvious to one skilled in the art are to be included within the scope of the following claims.
Number | Date | Country | Kind |
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10 2013 206 357.1 | Apr 2013 | DE | national |
This nonprovisional application is a continuation of International Application No. PCT/EP2014/057328, filed Apr. 10, 2014, which claims priority to German Patent Application No. 10 2013 206 357.1, filed Apr. 11, 2013, both of which are herein incorporated by reference.
Number | Date | Country | |
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Parent | PCT/EP2014/057328 | Apr 2014 | US |
Child | 14862603 | US |