Abstract:
An evaporator ( 1 ), for evaporating a liquid ( 4 ), particularly for a waste heat utilization device of an internal combustion engine, includes a plurality of channel plate arrangements ( 2 ) that are stacked in a stacking direction ( 3 ). A gas path ( 6 ) is formed between each pair of adjacent channel plate arrangements ( 2 ), through which a gas ( 7 ) can be conducted. The gas is used to supply the heat that is required to evaporate the liquid ( 4 ). Each channel plate arrangement ( 2 ) contains a liquid inlet ( 8 ), a steam outlet ( 9 ), and a channel ( 11 ) which connects the liquid inlet ( 8 ) and steam outlet ( 9 ) together and which forms a repeatedly-deflecting evaporation path ( 12 ) for the liquid ( 4 ) to be evaporated. Increased efficiency can be achieved if the channel ( 11 ) has, in an evaporation path ( 12 ) evaporation zone ( 14 ), a flowable cross-section ( 18 ) which increases in a direction of liquid ( 4 ) flow.

Description:
CROSS REFERENCE TO RELATED APPLICATIONS 
       [0001]    This application is a United States National Phase Application of International Application PCT/EP2012/062389 filed Jun. 26, 2012, the entire contents of which are incorporated herein by reference. 
     
    
     FIELD OF THE INVENTION 
       [0002]    The present invention relates to an evaporator for evaporating a liquid and to a waste heat utilization device for an internal combustion engine. 
       BACKGROUND OF THE INVENTION 
       [0003]    In waste heat utilization devices, which are based on the principle of a Rankine cycle process or a Rankine-Clausius cycle process, evaporators are employed with the help of which the working medium of the cycle process can be evaporated, for the purpose of which the heat required for that is extracted from the exhaust gas of an internal combustion engine. Accordingly, such an evaporator on the one hand comprises a gas path for the exhaust gas and on the other hand an evaporation path for the working medium to be evaporated. 
         [0004]    Such an evaporator can be configured for example as a plate heat exchanger and accordingly comprise multiple channel plate arrangements, which are stacked in a stacking direction, wherein in each case between two adjacent plate arrangements a gas path is formed, through which a gas can be conducted, via which the heat required for evaporating the liquid can be supplied. The respective channel plate arrangement in this case can practically contain a liquid inlet, a vapor outlet and a channel connecting the liquid inlet to the vapor outlet, which channel for example forms a repeatedly diverted evaporation path for the liquid to be evaporated. 
       SUMMARY OF THE INVENTION 
       [0005]    The present invention deals with the problem of stating an improved or at least another embodiment for an evaporator of the type mentioned at the outset, which is characterized by high efficiency and cost-effective producability. 
         [0006]    The invention is based on the general idea of designing the respective channel, in which the evaporation of the liquid takes place, at least in one evaporation zone of the evaporation path so that the cross section through which a flow can flow increases in the flow direction of the liquid to be evaporated. The cross section through which a flow can flow of the evaporation path which increases in the flow direction takes into account to a certain degree the increase in volume of the liquid to be evaporated through the evaporation. Because of this, an excessive pressure increase in the evaporation path for example can be avoided. Furthermore, the flow velocity in the gas phase can also be reduced, which increases the dwell time of the liquid to be evaporated in the evaporator. Altogether, the efficiency of the evaporator can be increased because of this. 
         [0007]    In conjunction with the plate design of the evaporator, the evaporator can be realized comparatively cost-effectively. The individual channel plate arrangements can be realized identical in design which reduces the production costs. 
         [0008]    The increase of the cross section of the evaporation path through which a flow can flow in this case can be effected without steps or gradually within the evaporation zone in the flow direction of the liquid to be evaporated, for example linearly or progressively. It is likewise possible to realize the cross-sectional increase in steps. 
         [0009]    The evaporation zone of the evaporation path substantially extends from a region of the evaporation path, in which evaporation commences, as far as to a region of the evaporation path, in which the liquid is substantially evaporated completely. 
         [0010]    According to an advantageous embodiment, the respective channel can comprise in a pre-heating zone a cross section through which a flow can flow which remains constant in the flow direction of the liquid. Here it is taken into account that no significant change in volume materializes in the pre-heating zone. The pre-heating zone substantially extends from the liquid inlet as far as to a region of the evaporation path, in which evaporation commences. 
         [0011]    Additionally or alternatively it can be provided that the respective channel in a superheating zone comprises a cross section through which a flow can flow which remains constant in the flow direction of the liquid. This is based on the consideration that in the superheating zone primarily a pressure increase in the vapor is to be achieved. The superheating zone in this case substantially extends from a region of the evaporation path, in which the liquid is substantially evaporated completely, as far as to the vapor outlet. 
         [0012]    If both in the preheating zone as well as in the superheating zone cross sections through which a flow can flow which remain constant are present, this means that the evaporation path has a cross section through which a flow can flow which increases in the flow direction only, i.e. exclusively, in the evaporation zone. This means, furthermore, that the cross section through which a flow can flow is larger in the superheating zone than in the preheating zone. 
         [0013]    In another embodiment, the respective channel can be formed through multiple channel sections arranged next to one another, wherein the evaporation path at the transition between two adjacent channel sections has a diversion of 180° each. Because of this, the channel or the evaporation path is given a meander-like course, which realizes a relatively great path length or channel length in a comparatively confined space. 
         [0014]    In another embodiment, the respective channel plate arrangement can comprise two plates, wherein the respective channel is formed through stampings, which are either formed only in one of the two plates or formed mirror-symmetrically in both plates. The stampings for this purpose can be configured in particular according to the channel sections in order to realize the meander-like course for the channel or the evaporation path. The stampings can be realized for example through deep-drawing or through high-pressure forming. Provided that the stampings are only formed in one of the two plates, the other plate can be configured flat. 
         [0015]    According to an advantageous further development, the respective plate provided with stampings can comprise on an outside facing the gas path convexly curved or flat contact surfaces in the region of the stampings. The curved contact surfaces can be produced in a particularly simple manner. The flat contact surfaces favor the through-flow in the gas path and can simplify the connection of elements improving the heat transfer. 
         [0016]    According to a practical further development, a fin structure can be arranged in the respective gas path which is arranged on the contact surfaces, in particular fastened thereon. Such a fin structure can improve the heat transfer between the gas of the gas path and the respective plate, which improves the heat-transferring coupling between gas path and evaporation path. The fin structure can for example be soldered or welded to the respective plate in the region of the contact surfaces. 
         [0017]    Particularly practically, the two plates of the respective channel plate arrangement can be fastened to one another. By doing so, the plate stack formed through the channel plate arrangements stacked on top of one another can be stabilized and in particular configured in a self-supporting manner. Practically, the two plates of the respective channel plate arrangement laterally enclosing the respective channel can be fastened to one another along the evaporation path. Because of this, the channels can be realized in a particularly simple manner. The fastening in this case can be realized for example by means of a soldering method or a welding method. Suitable welding methods are for example laser welding, microplasma welding, micro-TIG welding, roll seam welding and resistance welding. 
         [0018]    In another advantageous embodiment, two lateral boundary walls can be provided which limit the gas paths on sides located opposite one another from a gas inlet as far as to a gas outlet. The boundary walls in this case can connect to one another or fasten to one another the adjacent channel plate arrangements. The boundary walls thus increase the stability of the plate stack. The one boundary wall can comprise inlet openings, which are each fluidically connected to a liquid inlet of one of the channel plate arrangements. Because of this, the supply of the liquid to be evaporated through the boundary wall is simplified. The other boundary wall can comprise outlet openings, which are each fluidically connected to a vapor outlet of one of the channel plate arrangements. Thus, a common discharge of the evaporated liquid through the other boundary wall can be simplified. 
         [0019]    According to an advantageous further development, the boundary walls can each be formed through multiple wall elements, each of which laterally limit only one of the gas paths. Because of this, the modular construction of the evaporator is simplified, wherein in particular the number of the wall elements of the respective boundary wall largely corresponds to the number of the channel plate arrangements. Practically, the wall elements can each be attached either to both channel plate arrangements limiting this gas path or be integrally formed on one of the plates of one of the channel plate arrangements limiting this gas path and then be attached to the channel plate arrangement that is adjacent thereto. In particular, the integrated design, in which the respective wall element is integrally formed on at least one plate, simplifies a cost-effective production of the evaporator. Attaching the wall element is again practically effected via welded connections or soldered connections. By means of welded connections, multiple sheet seams can for example be realized, as a result of which multiple components can be fixed to one another simultaneously. Provided that the components to be fixed to one another lie flat against one another, soldered connections are preferred. 
         [0020]    In another advantageous further development, an inlet covering can be attached to the one boundary wall, which covers multiple or all inlet openings and forms a supply channel, which fluidically connects a common liquid connection to the liquid inlets. Additionally or alternatively, an outlet covering can be attached to the other boundary wall, which covers multiple or all outlet openings and forms a discharge channel, which fluidically connects a common vapor connection to the vapor outlets. Through this measure, the assembly of the evaporator or the installation of the evaporator in the waste heat utilization device is simplified. 
         [0021]    Practically, the stacked channel plate arrangements can form a stack which with respect to the stack direction has two end plates which are distant from one another, each of which form or limit a gas path with a channel plate arrangement that is adjacent thereto. The end plates thus do not contain an evaporation path but merely serve to limit the gas path. This design results in that all evaporation paths in the stack direction are arranged between two gas paths which increases the effectiveness of the evaporator. 
         [0022]    According to an advantageous embodiment it can be provided that the respective channel plate arrangement is produced from iron or an iron alloy, in particular from steel, preferentially from stainless steel. Because of this, the respective channel plate arrangement has a particularly high temperature resistance, as a result of which it is possible in particular to arrange the evaporator relatively near the engine block of the internal combustion engine in the exhaust system, e.g. on or in the exhaust manifold. Alternatively it is also possible in principle to produce the channel plate arrangements from a light metal, e.g. from aluminum, or from a light metal alloy, preferentially from an aluminum alloy, as a result of which the evaporator has a particularly high energetic efficiency. 
         [0023]    A waste heat utilization device according to the invention for an internal combustion engine, in particular in a motor vehicle, comprises a waste heat utilization circuit, in which a working medium circulates and in which in the flow direction of the working medium one after the other an expansion machine for expanding the working medium, a condenser for condensing the working medium, a conveying device for driving the working medium in the waste heat utilization circuit and an evaporator of the type described above for evaporating the working medium are arranged. 
         [0024]    An internal combustion engine according to the invention, in particular for a motor vehicle, comprises a waste heat utilization device of the type described above and an exhaust system, which is coupled in a heat-transferring manner to the evaporator of the waste heat utilization device. 
         [0025]    It is to be understood that the features mentioned above and still to be explained in the following cannot only be used in the respective combination stated but also in other combinations or by themselves without leaving the scope of the present invention. 
         [0026]    Preferred exemplary embodiments of the invention are shown in the drawing and are explained in more detail in the following description, wherein same reference characters relate to same or similar or functionally same components. 
         [0027]    The present invention shall be explained in more detail on the basis of the following figures and exemplary embodiments, without the present invention being limited to these. The various features of novelty which characterize the invention are pointed out with particularity in the claims annexed to and forming a part of this disclosure. For a better understanding of the invention, its operating advantages and specific objects attained by its uses, reference is made to the accompanying drawings and descriptive matter in which preferred embodiments of the invention are illustrated. 
     
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         [0028]    In the drawings: 
           [0029]      FIG. 1  is an isometric view of an evaporator; 
           [0030]      FIG. 2  is a longitudinal section through a channel plate arrangement of evaporator corresponding to section lines II in  FIG. 1 ; 
           [0031]      FIG. 3  is another longitudinal section of the channel plate arrangement according to section lines III in  FIG. 2 , showing one of different embodiments; 
           [0032]      FIG. 4  is another longitudinal section of the channel plate arrangement according to section lines III in  FIG. 2 , showing another of different embodiments; 
           [0033]      FIG. 5  is a longitudinal section of the evaporator in the region of multiple channel plate arrangements; 
           [0034]      FIG. 6  is a partly sectioned isometric view of a channel plate arrangement; 
           [0035]      FIG. 7  is an isometric view of a region of the evaporator; 
           [0036]      FIG. 8  is a sectional view through a region of the evaporator according to section lines VIII in  FIG. 7 , showing one of different embodiments; 
           [0037]      FIG. 9  is a sectional view through a region of the evaporator according to section lines VIII in  FIG. 7 , showing another of different embodiments; 
           [0038]      FIG. 10  is a sectional view through a region of the evaporator according to section lines VIII in  FIG. 7 , showing another of different embodiments; 
           [0039]      FIG. 11  is a sectional view through a region of the evaporator according to section lines VIII in  FIG. 7 , showing another of different embodiments; 
           [0040]      FIG. 12  is an isometric part view of a channel plate arrangement with fin structure; 
           [0041]      FIG. 13  is an isometric part view of the evaporator, showing one of different embodiments; 
           [0042]      FIG. 14  is an isometric part view of the evaporator, showing another of different embodiments; and 
           [0043]      FIG. 15  is a highly simplified schematic representation in the manner of a circuit diagram of a waste heat utilization device with such an evaporator. 
       
    
    
     DESCRIPTION OF THE PREFERRED EMBODIMENTS 
       [0044]    According to  FIG. 1 , an evaporator  1  comprises multiple channel plate arrangements  2 , which are stacked in a stacking direction  3 . The evaporator  1  serves for evaporating a liquid  4 , which can be supplied to the evaporator  1  according to an arrow. Preferably, the evaporator  1  is employed in a waste heat utilization device of an internal combustion engine in order to extract heat from exhaust gases of the internal combustion engine in order to thereby evaporator a liquid, namely a working medium of the waste heat utilization device. Such a waste heat utilization device operates according to the Rankine cycle process or according to the Rankine-Clausius cycle process. A substantial component of such a waste heat utilization device is the evaporator  1 , which creates a heat-transferring coupling between an exhaust system of the internal combustion engine and a waste heat utilization circuit of the waste heat utilization device. An example of such a waste heat utilization device is explained in more detail with reference to  FIG. 15  further down below. 
         [0045]    The stacked channel plate arrangements  2  form a plate stack  5  or evaporator lock  5 . Within the stack  2  or within the block  5 , a gas path  6  is formed in each case between two adjacent channel plate arrangements  2 , through which a gas  7  can be conducted corresponding to arrows. By way of this gas  7 , the heat required for evaporating the liquid  4  is supplied. The gas  7  in particular is exhaust gas of an internal combustion engine, the waste heat of which is to be utilized for example in a waste heat utilization device. 
         [0046]    According to  FIG. 2 , each channel plate arrangement  2  comprises a liquid inlet  8  and a vapor outlet  9 , through which vapor  10  or evaporated liquid can exit. Furthermore, the respective channel plate arrangement  2  comprises a channel  11 , which fluidically connects the liquid inlet  8  to the vapor outlet  9 . The channel  11  in this case forms a repeatedly diverted evaporation path  12  represented in dashed line for the liquid  4  to be evaporated. In the flow direction of the liquid  4  to be evaporated, the channel  12  initially comprises a preheating zone  13 , which is followed by an evaporation zone  14 , which is followed by a superheating zone  15 . Here, the preheating zone  13  substantially extends from the liquid inlet  8  as far as to a region  16  of the evaporation path  12 , in which evaporation of the liquid  4  commences. Within the preheating zone  13 , the liquid  4  is thus heated to its boiling temperature. The evaporation zone  14  substantially extends from this region  16 , in which evaporation of the liquid  4  commences, as far as to a region  17  of the evaporation path, in which the liquid  4  is substantially evaporated completely. Within the evaporation zone  14 , the liquid  4  substantially remains at its boiling temperature and is completely evaporated within the evaporation zone  14 . The superheating zone  15  substantially extends from the region  17 , in which the liquid  4  is substantially evaporated completely, as far as to the vapor outlet  9 . Within the superheating zone  15 , the temperature of the vapor  9  increases beyond the boiling temperature of the liquid  4 . 
         [0047]    The evaporator  1  introduced here is now characterized that within the respective channel plate arrangement  2  the respective channel  11  has a cross section  18  through which a flow can flow which at least in the evaporation zone  14  increases in the flow direction of the evaporating liquid  4 . In the shown embodiment of  FIG. 2 , the cross section  18  through which a flow can flow abruptly increases in multiple steps. In another embodiment, an increase of the cross section  18  that can be subjected to a through-flow can also be realized without steps or continuously. 
         [0048]    In the embodiment shown in  FIG. 2 , the cross section  18  through which a flow can flow is kept constant within the preheating zone  13 .d. Furthermore, in the embodiment shown in  FIG. 2 , the cross section  18  through which a flow can flow is kept constant within the superheating zone  15 . Thus, an increase of the cross section  18  in this case takes place only within the evaporation zone  14 . The cross section  18  through which a flow can flow is consequently smaller in the preheating zone  13  than in the superheating zone  15 . 
         [0049]    Practically, the respective channel  11  is configured meander-like in order to realize the repeatedly diverted evaporation path  12  in as compact as possible a manner. According to  FIG. 2 , the respective channel  11  for this purpose can be formed through multiple channel sections  19  which are arranged next to one another and separated from one another through joint channel walls  43 , which channel sections  19  are arranged on one another 19, so that the evaporation path  12  at the transition between two adjacent channel sections  19  is subjected to a 180° diversion in each case. For example, the liquid  4  or the vapor  10  flows through the individual channel sections  19  starting out from the liquid inlet  4  as far as to the vapor outlet  9  alternately from the bottom up or from the top down. 
         [0050]    According to the  FIGS. 3-14 , the respective channel plate arrangement  2  can each comprise plates  20 ,  21 , wherein the respective channel  11  and the channel sections  19  are formed through stampings  22 . These stampings  22  can be formed in both plates  20 ,  21  mirror-symmetrically according to  FIG. 3  or be formed in only one of the plates  20 ,  21  according to  FIG. 4 . In the example of  FIG. 4 , the one plate  20  is furnished with the stampings  22  while the other plate  21  is configured flat. 
         [0051]    The two plates  20 ,  21 , which between them form the channel  11  and the channel sections  19  respectively, are practically fixed to one another. Corresponding fastening locations are marked  23  in the  FIGS. 3 and 4 . These fastening locations  23  can be soldered connections or welded connections. The fastening locations  23  are practically embodied tight and are realized so that they laterally enclose the respective channel  11  and the respective channel section  19  and in particular form the channel walls  43 , so that ultimately the two plates  20 ,  21  are fastened to one another along the evaporation path  12 . 
         [0052]    The plates  20 ,  21  provided with the stampings  22  can be, on their outside, which within the block  5  faces the gas path  6 , be convexly curved or according to the  FIGS. 6-14  be configured flat in the regions of the stampings  22  according to the  FIGS. 3-5 . In the case of curved stampings  22 , curved contact surfaces  24  are created. Accordingly, in the case of the flat stampings  22 , flat contact surfaces  24  are created. 
         [0053]    According to the  FIGS. 1 ,  5  and  7 - 14 , a fin structure  25  can be arranged within the respective gas path  6  in order to improve the heat transfer from the gas flow  7  to the channel plate arrangements  2  and thus to the liquid  4  to be evaporated. The respective fin structure  25  in this case contacts the respective plate  20 ,  21  of the respective channel plate arrangement  2  facing the gas path. Practically, this contacting takes place in the previously mentioned contact surfaces  24 . Advantageously, according to  FIG. 5 , fixing of the fin structure  5  to the channel plate arrangements  2  in the region of the contact surfaces  24  can be additionally realized. Corresponding fastening locations are marked  26  in  FIG. 5 . Again, these can be soldering locations or welding locations. 
         [0054]    In order to improve the connection of the fin structure  25  to the channel plate arrangement  2 , the flat contact surfaces  24  are preferred. In particular, the fin structures  25  for this purpose can comprise a rectangular profile of a diamond profile transversely to the gas path  6  according to the  FIGS. 7-14  and accordingly likewise have flat contact surfaces, which are really in contact with the contact surfaces  24  of the channel plate arrangements  2 . 
         [0055]    According to the FIGS.  1  and  7 - 14 , the evaporator  1  comprises two lateral boundary walls  27 ,  28 , which limit the gas paths  6  on sides located opposite one another and thereby extend from a gas inlet  29  as far as to a gas outlet  30 . According to the  FIGS. 7 and 13 , the respective boundary wall  27  facing the beholder can comprise inlet openings  31 , which are each fluidically connected to a liquid inlet  8  of the respective channel plate arrangement  2 . The respective boundary wall  28  located opposite accordingly contains outlet openings which are not noticeable here, each of which is fluidically connected to a vapor outlet  9  of the respective channel plate arrangement  2 . 
         [0056]    In the embodiments of the  FIGS. 7-14  shown here, the two boundary walls  27 ,  28  are each formed through multiple wall elements  32 , wherein the individual wall elements  32  each laterally limit only one of the gas paths  6 . In the embodiment shown in  FIG. 8 , these wall elements  32  are designed as separate components with respect to the channel plate arrangements  2 , which are attached to the channel plate arrangement  2  limiting the respective gas path  6 . In contrast with this, the wall elements  32 , with the embodiments of FIGS.  7  and  9 - 14 , are integrally formed on one of the plates  20 ,  21  and attached to the adjacent channel plate arrangement  2 . Assembly in each of these cases is again effected via various fastening points  33  or  34 , which can be designed as soldered connections or welded connections. Purely exemplarily, multiple fastening points  33  are designed as multi-sheet seams, e.g. as three-sheet seams or four-sheet seams, while multiple other fastening locations  34  are designed as areal soldered connections. In the embodiments of the FIGS.  1  and  9 - 14 , the respective wall element  32  is integrally formed on the respective plate  21 , which is designed flat here and has no stampings  22 . In principle, however, any other embodiment is also conceivable. For example, two stamped plates  20 ,  21  can be provided. Alternatively, the wall elements  32  can be integrally formed on the plate  20  provided with the stampings  22 . 
         [0057]    In the embodiment shown in  FIG. 14 , an inlet covering  35  is attached to the boundary wall  27  facing the beholder, which covers multiple or preferentially all inlet openings  31  of the respective boundary wall  27  and forms a supply channel  36 , which fluidically connects a common liquid connection  37  to the liquid inlets  8  of the various channel plate arrangements  2 . Analogously to this, the other boundary wall  28 , according to  FIG. 1 , can also be equipped with an outlet covering  38  which covers multiple or preferentially all outlet openings of the respective boundary wall  28  on the outlet side and in the process forms a discharge channel  39 , which fluidically connects a common vapor connection  40  to the vapor outlets  9  of the respective channel plate arrangements  2 . 
         [0058]    As is evident furthermore from  FIG. 14 , the stack  5  or the block  5  respectively each comprise an end plate  41  and  42  respectively on ends which with respect to the stack direction  3  are distant from one another. The respective end plate  41 ,  42  limits in each case a gas path  6  in the stack direction  3  together with a channel plate arrangement  2  which is adjacent thereto. In said gas path  6 , a fin structure  25  can be additionally arranged. In the example of  FIG. 14 , the upper end plate  41  can be additionally formed integrally with two wall elements  32 , which jointly with the wall elements  32  of the channel plate arrangements  2  form the two boundary walls  27 ,  28 . 
         [0059]    The lower end plate  42  shown in  FIG. 14  is laterally overlapped by the wall elements  32  of the channel plate arrangement  2  adjacent thereto, as a result of which a sealed termination for the stack  5  or the block  5  can be easily realized. 
         [0060]    According to  FIG. 15 , an evaporator  1  according to the embodiments described above can be integrated in a waste heat utilization device  44 , with the help of which in an internal combustion engine  45 , heat contained in the exhaust gas can be utilized in order to thus improve the energetic efficiency of the internal combustion engine  45 . According to  FIG. 15 , such an internal combustion engine  45  comprises in the usual manner an engine block  46  with multiple combustion chambers  47  and a cooling block  48  for cooling the engine block  46 . The internal combustion engine  45  additionally comprises a fresh air system  49  for supplying fresh air to the combustion chambers  47 . A corresponding fresh air flow is indicated in  FIG. 15  by an arrow and marked with 50. Furthermore, an exhaust system  51  is provided, which discharges exhaust gas from the combustion chambers  47 . A corresponding exhaust gas flow is indicated in  FIG. 15  by an arrow and marked with 52. In the example, the internal combustion engine  45  is equipped furthermore with an exhaust gas turbocharger  53 , the turbine 54 of which is incorporated in the exhaust system  51  and the compressor 55 of which is incorporated in the fresh air system  49 . 
         [0061]    The cooling circuit  48  includes a radiator  56 , which is exposed to an airflow  57  indicated by arrow, which is generated or can be supported with the help of a fan  58 . A coolant pump  59  drives the liquid coolant in the cooling circuit  48 . 
         [0062]    The waste heat utilization device  44  comprises a waste heat utilization circuit  60 , in which a working medium circulates. In the waste heat utilization circuit  60  the evaporator  1  is arranged in such a manner that the working medium follows the evaporation path  12 . Downstream of the evaporator  1 , an expansion machine  61  is arranged in the waste heat utilization circuit  60 , which expands the compressed, evaporated and superheated working medium. In the process, the expansion machine converts heat or enthalpy into mechanical work and drives for example a generator  62  or G. The generator  62  in this case is electrically connected to an electrical energy storage unit  63 , which for example belongs to an electrical system  64  of the internal combustion engine  45  or of a vehicle, in which the internal combustion engine  45  is arranged. Downstream of the expansion machine  61 , a condenser  65  is arranged in the waste heat utilization circuit  60 , in which the expanded working medium is condensed. For this purpose, the condenser  65  comprises a heat exchanger or is configured as such. The condenser  65  can be incorporated in a cooling in a suitable manner. In the example, the condenser  65  is incorporated in the cooling circuit  48  of the internal combustion engine  45  in order to extract the heat from the working medium. It is clear that in another embodiment a cooling circuit which with respect to the engine cooling circuit  48  is separate can also be provided for discharging the heat from the waste heat utilization circuit  60 . Downstream of the condenser  65 , the waste heat utilization circuit  60  comprises a conveying device  66 , in particular a volumetric pump. The conveying device  66  serves for driving the working medium in the waste heat utilization circuit  60 . Here, the conveying device  66  operates against a pressure that can be adjusted with the help of the expansion machine. For driving the conveying device  66 , an electric motor  67  or M can be provided for example. The power supply of the electric motor  67  is practically effected with the help of the electrical system  64 , for the purpose of which a suitable power supply line  68  can be provided. 
         [0063]    While specific embodiments of the invention have been shown and described in detail to illustrate the application of the principles of the invention, it will be understood that the invention may be embodied otherwise without departing from such principles.