exemplary embodiments are shown in the fig1 a and 1 b , in which the circulating region is respectively embodied as a rotation circuit . fig1 a shows schematically the basic design of a first exemplary embodiment of a device according to the invention for the production of a metallic contact structure for electrically contacting a photovoltaic solar cell . starting at a paste reservoir 1 , paste is pumped via a pumping means 2 , embodied as a pump , through a particle filter 3 into a pressure means 4 . a portion of the paste is separated at the pressure means 4 at a plurality of branching points and via dispensing openings , respectively allocated to the branching points , applied on a carrier substrate 5 . the carrier substrate 5 represents a precursor of a solar cell to be produced from a silicon wafer , with on the side , shown at the top in fig1 , a metallic contact structure shall be applied . starting at the pressure means , the paste flows via an additional line back into the paste reservoir 1 . the paste reservoir 1 is refilled via a refill line 6 when the fill level falls short of a predetermined minimum value . as discernible in fig1 a , in the exemplary embodiment the paste present in the device according to the invention is in constant circulation : starting from the paste reservoir 1 , the paste is circulated via the pressure means and therefrom further downstream back to the paste reservoir . additionally , an agitator 7 is applied in the paste reservoir , which additionally leads to a local circulation within the paste reservoir . the pressure means 4 is embodied such that the rotating circuit at the outlet side of the pressure means is embodied as a throttle by way of a constriction of the cross - section . the pump 2 is embodied such that at the pressure side of the pump 2 a paste pressure is given of approximately 35 bar . this paste pressure increases only to a minor extent between the outlet side of the pump 2 via the particle filter 3 to the throttle unit at the outlet side of the pressure means 4 ( by less than 1 bar ). downstream in reference to the pressure means , however , in the return to the paste reservoir , a paste pressure is given only slightly above the ambient pressure . in the paste reservoir 1 approximately ambient pressure is given . the particle filter 3 is embodied in order to filter out undesired particles with their diameter exceeding 25 % of the minimum cross - section in the overall paste circuit ( including the dispensing openings ) so that any clogging of the dispensing openings of the pressure means is avoided . the device according to fig1 a further comprises two valves 9 as well as a bypass line 10 . by opening a first valve 9 and closing a second valve 9 or vice versa the paste flows in the rotation circuit optionally through the pressure means 4 or through the bypass line 10 . this way , an interruption of the application of paste trails onto the carrier substrate 5 is possible by switching the rotation circuit via the bypass line 10 , circumventing the pressure means 4 . furthermore , in the rotation circuit , downstream in reference to the pressure means 4 , a controllable throttle 11 is arranged so that on the one hand via the flow rate of the pump 2 and on the other hand via the control of the throttle effect of the throttle 11 the pressure in the rotation circuit can be adjusted , particularly between the pump 2 and the throttle 11 as well as in the pressure means 4 . fig1 b shows schematically the basic structure of a second exemplary embodiment of a device according to the invention for the production of a metallic contact structure for electrically contacting a photovoltaic solar cell . the second exemplary embodiment is equivalent with regards to design and function to the exemplary embodiment shown in fig1 a , with additionally here a second pump 2 ′ being arranged in the rotation circuit downstream in reference to the throttle 11 . this way , on the one hand additionally the pressure reduction in the pressure means 4 can be controlled by selecting different flow rates between the pump 2 and the pump 2 ′, and furthermore there is a reduced risk of clogging , particularly of the pipelines between the pressure means 4 , downstream thereat via the throttle 11 [ and the ] pump 2 ′ to the reservoir 1 , due to the additional feeding by the pump 2 ′. fig2 a shows a cross - section parallel in reference to the direction of flow of the paste in the rotation circuit of the pressure means 4 . the direction of flow of the paste in the rotation circuit extends from the left towards the right . the pressure means 4 is embodied as a hollow body , which shows several openings at the bottom , with two of them being marked as examples with the reference characters 8 ′ and 8 ″. the openings 8 ′, 8 ″ are embodied as penetrations of the external wall of the pressure means 4 . at the upper side of the openings 8 ′, 8 ″ in fig2 , a portion of the paste is respectively separated from the rotation circuit , flows through the openings , and is discharged to the end of the openings located at the bottom in fig2 , and this way several paste trails are applied on the carrier substrate 5 . in the upper section the openings therefore represent branching points for taking a portion of the paste from the rotation circuit , comprise in the lower section respective dispensing openings for discharging the paste , and between the branching point and the dispensing opening the openings serve as dispensing flow paths between the branching point and the dispensing opening . the cross - sectional area of the pressure means 4 in the area of the openings amounts to approx . 30 mm 2 . downstream in reference to the last opening the pressure means 4 shows a cross - sectional constriction in the area a towards a cross - sectional area at the outlet side of the pressure means 4 of 6 mm 2 . this cross - sectional constriction in the area a acts as a throttle for the paste in the rotation circuit so that the above - mentioned pressure ratios develop . the openings 8 ′, 8 ″ of the pressure means 4 are embodied cylindrical with a cross - sectional area of 0 . 018 mm 2 . due to the considerably larger cross - sectional area of the pressure means 4 in the rotation circuit of the paste , compared to the cross - sectional areas of the openings 8 ′, 8 ″, the pressure reduction amounts to only 0 . 015 bar , from the first opening 8 ′ to the last opening , seen in the direction of flow of the plate in the rotation circuit . at the upper sections of the openings 8 ′, 8 ″, i . e . at the branching points , therefore an approximately constant pressure is given , so that this way already an approximately constant volume flow is ensured at the dispensing openings of the pressure means 4 . in order to compensate the above - mentioned low pressure difference , additionally the lower conversion of the pressure means 4 is embodied , with regards to the wall thickness , seen in the direction of flow of the paste in the rotation circuit , from the first opening 8 ′ reducing towards the last opening , seen in the direction of flow of the paste in the rotation circuit . this way , a continuously reducing length of the openings develops . openings with greater length and accordingly longer flow paths between the branching point and the dispensing opening therefore show a slightly increased flow - through resistance for the paste so that the above - mentioned pressure reduction is additionally compensated by the flow - through resistance reducing with shortened length of the opening . this way , a homogenous volume flow is achieved very precisely in all dispensing openings for the paste dispensed . fig2 b shows a second exemplary embodiment of a pressure means 4 ′ in a cross - section parallel in reference to the direction of flow of the paste in the rotation circuit . in this exemplary embodiment the pressure means shows no enlargement at the inlet and / or tapering of the diameter at the outlet , but it is embodied with the diameter of the tubular thickness of the rotation circuit . fig2 c shows a third exemplary embodiment of a pressure means 4 , also in a cross - section , parallel in the direction of flow of the paste in the rotation circuit . in this exemplary embodiment the thickness of the conversion is embodied reducing in the area of the openings 8 ′, 8 ″, 8 ′″ in the direction of flow of the paste so that the flow path of the paste reduces from the branching point of the rotation circuit to the dispensing opening , i . e . the flow path at the opening 8 is greater than at the opening 8 ′ and this in turn greater than at the opening 8 ′″, etc . by the reducing flow path the flow resistance is also reduced and thus the pressure reduction in the pressure means 4 is compensated over the rotation circuit . fig3 a shows a cross - section perpendicular in reference to the drawing level in fig2 , along the line a . the pressure means 4 is embodied as a hollow cylinder , with at least in the area of the openings 8 ′, 8 ″ the wall thickness of the hollow cylinder , as described above , is embodied reducing in the direction of flow of the paste in the rotation circuit . fig3 b , 4 a , and 4 b show alternative embodiments of pressure means each in a cross - section perpendicular in reference to the drawing level in fig2 along the line a . in the exemplary embodiment according to fig3 b , in the circumferential direction of the pressure means , two openings each are arranged , so that not only in the direction of the rotation circuit simultaneously several paste trails are applied , but additionally also perpendicular in reference to the circulating direction two paste trails each are applied simultaneously , for example in order to generate two paste trails located over top of each other in order to increase the aspect ratio . fig4 a and 4 b illustrate exemplary embodiments similar to fig3 a and 3 b , with the pressure means showing a rectangular cross - section . when embodying the pressure means 4 with a rectangular cross - section a bottom plate , which comprises openings 8 , can be exchanged in a simple fashion in order to quickly make corrections , for example in case of clogging , and / or select different arrangements for various fields of application , a different number and / or a different size of openings by using an appropriate bottom plate . fig4 shows an alternative embodiment of a pressure means 4 . the pressure means 4 is embodied box - shaped , comprising a u - shaped element , which is closed by a bottom plate 4 b . openings 8 are formed in the bottom plate 4 b . in this embodiment , by exchanging the base plate an adjustment of the design of the openings 8 can be implemented in a simple fashion , for example to different viscosities of the paste . fig5 shows another exemplary embodiment of a pressure means 4 , with only a detail of a cross - section in the area of the opening 8 ′ being shown . the opening 8 ′ is embodied like a nozzle at the exterior of the pressure means 4 . this way , nozzle geometries of prior art can be integrated in a simple fashion in the device according to the invention in order to generate particular geometries of the paste trails and this way further increase the aspect ratio of the paste trails generated . fig6 shows a perspective illustration of the pressure means 4 and several carrier substrates 5 during the production of the metallic contact structure . the carrier substrates 5 are moved underneath the locally fixed pressure means 4 according to the direction d . this way , via the openings 8 ′, 8 ″ of the pressure means 4 several parallel paste trails are generated on the carrier substrate 5 , from which the finger - like metallic contact structures , known per se , are formed on the carrier substrate 5 . fig7 shows another exemplary embodiment of a device according to the invention , in which several pressure means 4 , 4 a , 4 b are arranged parallel in reference to each other . the carrier substrates 5 are moved according to the direction d and the openings of the pressure means 4 , 4 a , and 4 b are arranged such that paste trails are created positioned over top of each other . thus , three paste trails are created , located over top of each other on the carrier substrate 5 , so that an additional increase of the aspect ratio is achieved . fig8 a shows another exemplary embodiment of the device according to the invention in a schematic detail . here , one pumping means 2 ″ and 2 ′″ is respectively allocated to each outlet of the pressure means 4 . via this pumping means the paste is moved back and forth in an oscillating fashion in the pressure means 4 , as marked by the arrows in fig8 . this way , a constant movement of the paste and thus a shearing stress upon the paste is also achieved , which leads to an advantageous , simpler processing of the paste . in this exemplary embodiment it is therefore not necessary to form a closed circuit because the circulation occurs in this case by a linear oscillating motion of the paste . preferably containers are provided at the outlets of the pumping means 2 ″ and 2 ′″, each at the side facing away from the pressure means 4 , to collect and / or refill the paste . fig8 b shows another exemplary embodiment of the device according to the invention which comprises a refill line 6 , a paste reservoir 1 with an agitator 7 , pressure means 4 , as well as pumping means 2 ″ and 2 ′″. the two above - mentioned pumping means are on the one side connected in a fluid conducting fashion to the paste reservoir 1 and on the other side via filters 3 ″ and 3 ′″ as well as via valves 9 ″ and 9 ′″ in a fluid conducting fashion to the pressure means 4 . in this exemplary embodiment it is therefore possible to achieve an oscillating movement of the paste back and forth in the pressure means 4 . additionally it is possible by the concordant pumping of the paste via the pumping means 2 ″ and 2 ′″ to convey the paste in the rotation circuit . potentially developing particle collections can be dissolved by reversing the circulation circuit . fig9 shows another alternative exemplary embodiment of a pressure means 4 ′″. fig9 a shows the pressure means 4 ′″ in a cross - section perpendicular in reference to the direction of flow of the paste , with the cylindrical tubular paste line 12 being connected via a displaceable nozzle bar 13 to a respective branching point and a dispensing opening in said nozzle bar 13 in a fluid - conducting fashion . a detail b of the nozzle line 13 is shown in a perspective in fig1 . here , a plurality of openings is visible , which open in branching points , each of which opens at the bottom of the nozzle bar 13 , not shown , in a dispensing opening . using a motorized displacement means , not shown , the nozzle bar 13 in fig9 a can be shifted horizontally , as indicated by the arrow . this way it is possible to provide a new nozzle , i . e . a new branching point with a dispensing opening , in a simple fashion and particularly also in an automated fashion by a simple linear shifting of the nozzle bar when a nozzle is clogged . this way , the maintenance expense of the device according to the invention is considerably reduced and in particular it is possible to yield low downtimes caused by clogged nozzles . in the illustrated details b and c of fig9 other views of the pressure means 4 ′″ are shown : fig9 b shows a side view parallel in reference to the direction of flow of the paste in the tubular paste line 12 , i . e . a view according to arrow b in fig9 a and perpendicular in reference to the drawing level in fig9 a . here , particularly at the bottom of the pressure means 4 ′″, receivers 15 are discernible in which for example one nozzle bar 13 each can be inserted according to fig1 b , with the direction of displacement in fig9 b being perpendicular in reference to the drawing level . the receivers 15 are complementary to the cross - sectional shape of the nozzle bars to be accepted therein , so that the nozzle bars can be arranged in the receivers in a form - fitting fashion . fig9 c shows as a detail a view of the bottom of the pressure means 4 ′″. here , openings of the pressure means 4 ′″ 16 are each discernible in the receivers 15 , from which during operation paste is dispensed and passes through the respective openings in the nozzle bar through the respective nozzle bar in order to reach the carrier substrate ( not shown ). as an alternative to the use of nozzle bars 13 here nozzle platelets 14 may be used according to fig1 a . these nozzle platelets only show one opening and are exchanged if necessary , for example when an opening is clogged . here , advantageously an automatic dispenser , comprising a magazine with a plurality of nozzle platelets 14 , is arranged at the pressure means 4 ′″ so that optionally a nozzle platelet can be exchange , which is located in a predetermined receiver 15 , by way of inserting a new nozzle platelet 14 using the dispenser . the nozzle platelets 14 and / or the nozzle bar 13 may be produced from different materials , preferred materials are ceramics , silicon , or steel . as particularly discernible in fig9 a and 9 b , the nozzle platelets 14 and / or the nozzle bar 13 represent the lowest point of the pressure means 4 ′″ when arranged in the receiver 15 . this is ensured in that the end ( reference character e in fig1 a and e ′ in fig1 b ) of the nozzle platelet 14 and / or the nozzle bar 13 pointing downwards is embodied such that it projects downwards after being inserted into the receiver 15 . this is illustrated in the exemplary embodiment shown in fig1 a and 10 b by the nozzle platelet 14 and the nozzle bar 13 showing a dovetail shape in its cross - section . preferably the nozzle platelets 14 or the different openings of the nozzle bar 13 vary with regards to the length of the nozzle channel : in fig1 a ′, as an example , a cross - section through the nozzle platelet 14 perpendicular in reference to the longitudinal extension of the nozzle platelet is shown , centrally in reference to the opening in the nozzle platelet . in the lower section a nozzle channel 17 is provided which shows the optimal length and the optimal diameter for the desired dosing behavior of the paste . in the upper section a supply channel 18 is provided which bridges the remaining height of the nozzle platelet 14 and furthermore shows a considerably larger diameter compared to the nozzle channel 17 , preferably at least twice , preferably at least tenfold the diameter of the nozzle channel 17 . the supply channel 18 and the nozzle channel 17 are each embodied cylindrical . this way it is possible to provide nozzle channels with different lengths and different diameters at a constant height of the nozzle platelet 14 , so that the dosing behavior can be varied by a selection of different lengths and diameters of the nozzle channel 17 . of course , it is also possible to embody different openings according to the cross - sectional illustration 10 a ′ at the nozzle bar 13 and particularly to vary the length and diameter of the respective nozzle channel between the individual openings of the nozzle bar . this way when using the nozzle bar 13 the dosing behavior can be influenced by displacing said nozzle bar . an exchange between two nozzle platelets 14 or two different openings of the nozzle bar 13 occurs preferably simultaneously with the exchange of the carrier substrate to be processed .