table 1 shows the material specifications of an exemplary laminar evaporator in accordance with the invention . according to this the laminar evaporator consists of six layers : a metal foil and five metal wire meshes sintered onto it . the metal in the present example consists of the heat - conducting alloy nicr8020 , din material number 2 . 4869 . different heat - conducting alloys could of course also be used . heat - conducting alloys can be ordered as starting material from the company thyssenkrupp vdm gmbh , www . thyssenkruppvdm . de , and then processed into foils , fine wires and wire meshes . thyssenkrupp vdm gmbh supplies the previously mentioned material nicr8020 , din material number 2 . 4869 , under the trade name “ cronix 80 ”, which can also be fused to a very pure specification with a carbon content & lt ; 0 . 02 %. the company record metall - folien gmbh , www . recordmetall . de , in co - operation with its suppliers , is in a position to make available metal foils from a thickness of 5 μm from starting material preferably in the form of strip . the company j . g . dahmen & amp ; co . gmbh & amp ; co . kg , www . dahmen - draht . de , is able to draw fine wires starting from a thickness of 18 μm from starting material preferably in the form of wire . the fine wires can subsequently be routinely woven into wire mesh by wire weaving mills , for example by the companies haver & amp ; boecker , www . haverboecker . com , or sporl kg , www . spoerl . de . the metal foil and the wire mesh layers are connected by sintering . sintering preferably takes place under vacuum or under a protective atmosphere of hydrogen . such sintering counts as state of the art and can be routinely carried out , for example , by the company gkn sinter metals filters gmbh , www . gkn - filters . com , as well as by the company sporl kg , www . spoerl . de . sintering is advantageously effected in the form of multiple cutouts ; that is , the individual laminar evaporators are not sintered , but larger area cutouts are used , for example in the format 200 × 200 mm . the individual laminar evaporators are obtained from the multiple cutouts after sintering by laser cutting or stamping machines . instead of heat - conducting alloys , stainless steels , e . g . aisi 304l or aisi 316l , are also used as alternative materials for the laminar evaporator in accordance with the invention . these have substantial cost advantages over nicr8020 , but nevertheless have a distinctly lower electrical resistance compared with nicr8020 . to increase the electrical resistance the stainless steel laminar evaporators or the intermediate products of which they are made — the multiple cutouts — can optionally be etched . material is evenly removed by etching . the etching can advantageously be carried out in an aqueous pickling bath consisting of 50 % nitric acid and 13 % hydrofluoric acid . such pickling baths can be supplied under the designation “ avesta 302 ” by the company avesta finishing chemicals , www . avestafinishing . com . a favorable side effect of the etching is that it also increases the porosity of the laminar evaporator somewhat , as a result of which the evaporator becomes more absorptive for the material to be evaporated . however , the additional process step of etching at least partly reduces the original cost advantages compared with heat - conducting alloys . an interesting option also consists of combining heat - conducting alloys and stainless steels , where preferably the more substantial layers consist of a heat - conducting alloy and the finer layers of stainless steel . in the specific example in accordance with table 1 , this option could mean , for example , that the three outside layers , namely layers 3 to 5 , could be made of stainless steel . with laminar evaporators constructed in accordance with table 1 the porous structure is formed by sintering the wire mesh layers with one another . both the wire mesh layers and the metal foil make a contribution to the resulting electrical resistance heater . the values for specific electrical resistance and for the heat conductivity stated in table 1 are of course valid in the surface direction . the values decrease disproportionately as the porosity increases . fig1 shows an example of a rectangular arrangement of a laminar evaporator 1 . the dimensions of the evaporator amount to : length = 12 mm , width = 5 . 6 mm . the structure of the evaporator corresponds to that of table 1 . the evaporator and / or its electrical resistance material is electrically contacted at its narrow ends , thus forming two poles 2 , 3 at these ends , over which the heating current is fed in and out . the heating current flows as soon as a voltage is applied to the poles 2 , 3 . the arrangement shown in fig1 can also represent only a heated or heatable cutout of a laminar evaporator 1 . the resistance material , including the porous structure , can continue outside via the poles 2 , 3 . for example , the laminar evaporator 1 can be contacted beyond the poles 2 , 3 , preferably on the foil side , by means of an electrically conducting adhesive or by a welded joint , which at the same time also effects a mechanical attachment of the evaporator . the linear poles 2 , 3 would in this case represent the outside boundary of laminar contact . as can be easily checked , the resulting heat resistance of the laminar evaporator shown in fig1 amounts to 81 mohm . fig1 furthermore shows the lines of flux 4 of the original electric field forming between the poles 2 , 3 , if a voltage is applied to the poles 2 , 3 . consequently , the lines of flux run in a straight line and connect the two poles in the shortest way . the evaporator arrangement shows an absolutely homogeneous current and power density distribution . fig2 shows the same laminar evaporator as fig1 , but now with slot - shaped recesses 5 in accordance with the invention . the recesses 5 are aligned at right angles to the lines of flux 4 of the original electric field ( see fig1 ), as a result of which these lines of flux are constricted . the constricted lines of flux are marked in fig2 by the reference symbol 6 . altogether nine slots 5 are provided . the slots are formed as cuts in the specific example . the length of the cuts is 1 . 2 mm . the cuts 5 proceed from opposite edges 7 of the laminar evaporator 1 . the cuts can advantageously be made by means of an nd : yag laser . with this cutting procedure , cuts with a width of 50 μm , for instance , can be made . the advantages of such fine cuts have already been shown earlier . by the cuts 5 the resulting heating resistance of the laminar evaporator rises to 110 mohm , i . e . an increase of approximately 35 %. the constriction of the electrical lines of flux 6 entails an uneven distribution of the electric field strength . specifically , in zone 9 directly bordering the ends of 8 of the cutouts 5 , where the lines of flux are most strongly constricted , particularly high field strengths arise almost selectively , while in the zones 10 bordering the cuts 5 the field strength exhibits comparatively low values . since the field strength enters the calculation of the electric power density as a square , it can be expected that the electric power density will vary even more , which fig3 shows to be the case . in broad terms , three zones can be differentiated : on the one hand immediately adjacent to the ends of the cuts 5 and again almost selectively zones 11 of the highest power density ( shown in black ); on the other hand , two border zones 12 a and 12 b of the lowest power density extending over the long sides of the laminar evaporator 1 , which extend in the width direction approximately up to the ends of the cuts 5 ( shown in white ); and finally a central zone 13 of medium power density , which essentially extends between the edge zones 12 a and 12 b ( shown dotted ). this markedly non - homogeneous power density distribution together with the poor heat conductivity of the porous structure also results in the formation of steep temperature gradients during the pulse heating in the porous structure and concomitantly in the material to be evaporated . the following arithmetical example and the results from it are based on the evaluation of the heat conductivity equation for the geometry shown in fig2 and on the conditions in accordance with tables 2 and 3 . table 2 describes the composition of the material to be evaporated . accordingly , the material in the specific example consists of a nicotine solution highly diluted with ethanol and water . glycerol is used as an aerosol former . furthermore a range of organic acids are added to protonate the nicotine . the pores of the porous structure are completely filled with the nicotine solution , as a result of which a total of 10 . 4 μl nicotine solution is stored in the porous structure . the material released in the course of the evaporation is essentially determined by the ternary system ethanol - water - glycerol . the task of releasing the ingredients set out in table 2 as synchronously as possible will succeed if the two groups of main materials , the solvent ( ethanol and water ) on the one hand and the aerosol former ( glycerol ) on the other hand , are released as synchronously as possible . the fact that this task is not simple can be seen from the substantially different material properties of these groups of materials alone — see table 2a . in solving the heat conduction equation the electric power density shown in fig3 is entered as the heat source . to calculate the power density a dc voltage of 1 . 5 v applied to the poles 2 , 3 was taken as a basis , where the current is supplied with a variable duty cycle in accordance with table 3 . in this way the energy input can be controlled as desired throughout the pulse heating and evaporation . the resulting useful voltage is thus a square wave signal of constant amplitude but with a variable pulse duty factor . furthermore , the temperature was constant at the poles 2 , 3 at an ambient temperature ( 20 ° c . ), which broadly also applies if the laminar evaporator 1 is at the same time also attached to the poles . fig4 shows as a first result of the evaluation the temperature distribution in the cross section a - a in accordance with fig3 , 0 . 5 and / or 1 . 0 seconds after the start of pulse heating . according to this , temperature gradients in the order of magnitude of 200 ° c ./ mm , and even up to 350 ° c ./ mm in some cases , occur in the porous structure and hence also in the nicotine solution . these values are already quite near enough to the temperature gradients arising in a glowing cigarette . fig5 shows as a further result of the simulation the quantities of solvents ( ethanol and water ) and aerosol former ( glycerol ) released cumulatively during pulse evaporation . the values are proportional and refer to the starting quantities originally stored in the porous structure . in the calculation it was assumed that the release of the individual components of the ternary system ethanol - water - glycerol is only temperature - dependent and that this dependence can to a close approximation be recorded by an exponential law . the upper curve represents the solvent , the lower curve the aerosol former . fig6 , in direct comparison to this , shows the material release on using a laminar evaporator , as shown in fig1 , hence without any slots , where the voltage applied to the poles 2 , 3 was reduced to 1 . 3 v ( same power density ) because of the now lower heating resistance . it is possible to see immediately how substantial is the influence of the slot - shaped recesses and / or cuts 5 on the dynamics of the release . the material release in accordance with fig5 runs extremely synchronously while the solvent and the aerosol former in the example in accordance with fig6 are released in almost the opposite direction . from this it may be concluded that the slit laminar evaporator 1 in accordance with fig2 appears substantially better suited for supplying a systemically active substance via the lung alveoli , in the specific example of a systemic nicotine administration , than an evaporator without such slots . the slot length must be adjusted to the specific material properties of the laminar evaporator , in particular to the heat conductivity of the porous structure , where in the long run a compromise must be found : excessively long slots and / or cuts lead to zones being formed locally with no or very little evaporation . the material to be evaporated is only slightly heated in such zones . such zones can also be called dead zones , because they play little or no part in the evaporation . if the slot length is made too short , however , the potential of the slot to form steep temperature gradients will not be exploited to the fullest extent . the supply of the laminar evaporator 1 with electric current in accordance with fig2 can be by means of a rechargeable battery . in the current state of the art , lithium ion as well as lithium polymer cells in particular are offered for this purpose . these cell types at present offer the highest power densities and flows and have been widely used for a long time , where mention should be made particularly of their widespread use in mobile phones . if two laminar evaporators 1 in accordance with fig2 are electrically connected in series and the energy supply is effected on the basis of an individual lithium polymer cell with a nominal or an open circuit voltage of 3 . 7 v and a working voltage under a load of approximately 3 v , then the current which flows through the laminar evaporators is calculated as 13 . 6 a on the basis of ohm &# 39 ; s law . this amperage can be drawn from today &# 39 ; s lithium polymer cells without any problem . cell type slpb533459h4 from the manufacturer kokam co ., ltd ., www . kokam . com , can be cited as an example . the dimensions of the cell are : 58 . 5 . times . 33 . 5 . times . 5 mm ( l × b × h ) with a weight of 19 . 5 g . the cell has a capacity of 740 mah and is able to supply a continuous current of 14 . 8 a . if one takes a pulse current flow according to table 3 as a basis , then the two evaporators , connected in series , draw a quantity of electricity of around 4 . 4 mah per pulse evaporation . therefore up to 168 evaporation cycles and / or inhalations would theoretically be possible with the above - mentioned kokam cell . this value may well not be fully achieved because of the relatively high amperage and the pulsed nature of the current requirements . the cell mentioned can , however , be recharged very quickly . fig7 a and 7b show an evaporator arrangement within an inhaler component , where the laminar evaporator 1 is identical in geometry and structure to the arrangement in accordance with fig2 . the laminar evaporator 1 is connected preferably on the foil side to two end sections on two electrically conducting plate - shaped contact elements 14 a and 14 b , with the surface of which it is also at the same time in electrical contact . contact can take place , for example , via a laminar adhesive joint by means of a conductive adhesive , e . g . from the company epoxy technology , www . epotek . com . the filament current flows as soon as a voltage is applied to the contact elements 14 a and 14 b . since the electrical conductivity of the contact elements 14 a and 14 b is many times greater than the conductivity of the laminar evaporator 1 , the outside boundaries 15 a and 15 b of the contact elements , that is those places in which the laminar evaporator 1 first touches the contact elements 14 a and 14 b , can be understood as poles 2 , 3 . the pole 2 is suggested in fig7 a by a thick line . the laminar evaporator 1 extends with an end section into a capillary gap 16 . the capillary gap 16 is formed by the contact element 14 b and an upper section 17 disposed on this superficially , by forming a corresponding recess , e . g . a milled slot , in the upper section 17 . the capillary gap 16 communicates with a liquid reservoir 18 ( shown symbolically in fig7 ). the liquid reservoir 18 contains the material to be evaporated and / or the liquid to be evaporated 19 . the liquid 19 could consist , for example , of a diluted drug preparation ; such a preparation has , for example , already been described in table 2 . furthermore , a ventilation hole 20 is provided in the contact element 14 b , which likewise communicates with the liquid reservoir 18 . the arrangement has the following effect : the capillary gap 16 draws liquid from the liquid reservoir 18 as a result of the capillary forces working in it , so that the capillary gap 16 fills with liquid 19 . the liquid 19 comes into contact with the porous structure of the laminar evaporator 1 in the capillary gap 16 . the porous structure is moistened by the liquid 19 and for its part acts like a wick , so that the entire porous structure of the laminar evaporator 1 fills automatically with the liquid 19 . to balance the quantity of the liquid taken , air flows from the environment through the ventilation hole 20 into the liquid reservoir 18 . after every pulse heating and evaporation of the liquid 19 the filling procedure is repeated . the porous structure in this case acts multi - functionally : first of all the porous structure supports the formation of steep temperature gradients in the liquid 19 to be evaporated because of its low heat conductivity ; secondly it holds the liquid 19 in its pores during the evaporation , so that an exchange of material in the surface direction is prevented and temperature gradients already formed are not disturbed ; and thirdly after pulse evaporation it automatically refills with the liquid to be evaporated 19 as a result of the capillary forces acting in it . the supply of the capillary structure with the liquid 19 to be evaporated takes place in the example in accordance with fig7 a in the direction of the lines of flux 4 of the original electric field ( see fig1 ). the slot - shaped recesses and / or cuts 5 are arranged staggered one behind the other aligned in two rows substantially parallel to the lines of flux . this creates a central main supply vein 21 reserved for the wick , which is to a large extent free from slot - shaped recesses and over which the porous structure can be supplied with the liquid 19 to a large extent unhindered ( suggested in fig7 a by an arrow ). fig8 a and 9b show a circular evaporator arrangement . the laminar evaporator 1 is again constructed as shown in table 1 and is again supplied in this example via a capillary gap 16 with the liquid 19 to be evaporated . in contrast to the previous example the filling of the capillary structure here takes place transverse to the lines of flux of the original electric field and the slot - shaped recesses and / or cuts 5 point in the direction of feeding . specifically , the feeding takes place radially from the inside outwards ( suggested in fig8 by arrows ) and the cuts 5 are likewise radially aligned . this kind of feeding has the advantage that the capillary current in the wick is not obstructed by the cuts 5 . cuts are intended both at the inside and at the outside periphery . the cuts at the inner periphery form tongues 22 , which partly project into the capillary gap 16 and in this way cause the capillary coupling with the liquid 19 . the capillary gap 16 is formed by a printed circuit board 23 and a cover plate 24 placed on its surface , in that a corresponding recess , e . g . a milled slot , is formed in the cover plate 24 . the capillary gap 16 draws the liquid 19 to be evaporated from a liquid reservoir 18 ( represented symbolically in fig9 b ), and a ventilation hole 20 is also again intended to balance the pressure . electrical contact with the laminar evaporator 1 is made by two extensions 25 , by fastening the latter , preferably on the foil side , by means of a conductive adhesive to the printed circuit board 23 . the poles 2 , 3 are in each case suggested by a thick line in fig9 a . in selecting the materials for the construction units for forming the capillary gap 16 care should be taken to achieve good wettability of the same with the liquid to be evaporated 19 . this condition is valid both for the arrangement in accordance with fig7 a and 7b and for the arrangement in accordance with fig9 a and 9b . the structure of a laminar evaporator in accordance with the invention shown as an example in table 1 is based on the fact that several metal fabric layers are sintered onto a metal foil . with evaporators of this design the vapors formed can only exit from the porous structure on the side opposite the metal foil . as an alternative to this design laminar evaporators with the porous structure open on both sides can also be used where it is particularly advantageous if the resistance heating element is formed entirely of the porous structure . laminar evaporators of this design allow particularly high evaporation rates . such an evaporator can , for example , consist of an electrically conducting open - pored foam material . such foam material made of e . g . aisi 316l stainless steel can be obtained from the company mitsubishi materials corporation , www . mmc . co . jp . here the starting point was a standard foam material with a thickness of 0 . 5 mm , a pore diameter within the range 50 - 150 μm and a porosity of about 90 %. the material can be reduced by rollers as required to a thickness of , for instance , 100 μm . the consolidated material can subsequently still be sintered if required . the compression naturally also reduces the porosity , which can be increased again , however , if necessary in the course of a subsequent etching treatment . heat - conducting alloys , in particular from the group of nicr alloys , e . g . nicr8020 , din material no . 2 . 4869 , can be likewise converted to such a foam material . the laminar evaporator can consist of a single foam layer or of several foam layers sintered together . to increase the stability and strength of the laminar evaporator the foam can optionally be sintered onto a thin support layer , for example onto a wire mesh of stainless steel or a heat - conducting alloy . the laminar foam material can be made to any shape by laser cutting . the slot - shaped recesses and / or cuts in accordance with the invention are again preferably made in the foam material by means of an nd : yag laser . in all the foregoing examples shown the slot - shaped recesses and / or cuts proceed from the edges of the laminar evaporator . the invention is , of course , not limited to this arrangement . rather the slot - shaped recesses and / or cuts can also be disposed spaced apart from the edges . slots arranged in this way have a double - constricting effect , since in this case both ends of slit restrict the lines of flux of the original electric field .
the disclosure relates to a laminar evaporator including an electrical resistance heating element for pulse heating and evaporation of an inhalationally receivable material distributed or distributable on the heating element surface by an electric heating current flowing or flowable in a laminar manner with at least two electrical contacts or poles for introducing the heating current into the resistance heating element , wherein the resistance heating element has at least one slot - shaped recess constricting lines of flux of an original electric field forming or formable between the at least two electrical contacts or poles and comprises a porous structure having a porosity of 70 % or greater holding or capable of holding the material .