fig1 illustrates in a strictly schematic vertical longitudinal sectional view the structure of a tempering device . it contains as an essential component a tempering vessel 2 in vertical arrangement . an amount of mass 4 is present in an interior container 6 and is in heat exchange relation with a heat exchange medium , preferably water , which is circulated in a jacket space 8 between the interior container 6 and an outer container 10 . a conducting helix 12 is provided in the jacket space 8 to increase the flow velocity of the heat exchange medium and thus the uniformity of the heat transfer so that local temperature differentials within the mass 4 are avoided as far as possible . a retractable lid 14 which is also made double - walled and can be supplied with the heat exchange medium ( not shown ) closes the vessel 2 and bears a stirrer 16 driven by a gear motor 18 , a probe body 20 immersed into the mass 4 and serving for measuring the temperature of the mass and possibly also other values of state , and further devices , if required , which are not illustrated in fig1 . during and after the tempering process , the mass 4 is continuously recycled between a discharge conduit 22 via a first three - way valve 24 , a mass pump 26 , a recirculating circuit 28 , a second three - way valve 30 , and a back flow conduit 32 . all these parts are , as well as the vessel 2 , surrounded by jacket spaces 34 through which the heat exchange medium is circulated , and a heat insulation 36 surrounds the vessel 2 and the said parts to eliminate as far as possible any disturbances of the tempering process by ambient temperature influences and heat losses . a heated feed conduit 38 is provided to supply mass to the vessel 2 . the vessel can be emptied via the three - way valve 24 through an outlet 40 , and a discharge line 42 is provided for delivering tempered mass and may be fed by a corresponding setting of the second three - way valve 30 . the heat exchange medium , preferably water , serves for heating and cooling of the mass . it is circulated in its own recirculation path : from the outlet of a recirculation pump 44 , a heat exchange medium feed line 46 is fed which opens into the lower range of the jacket space 8 of the vessel 2 via a plurality of outlet openings 48 . the heat exchange medium flows upwards in the vessel jacket space , under conduction of the conducting helix 12 , and then flows via an overflow container 50 through the jacket spaces 34 of the second three - way valve 30 of the mass pump 26 and the first three - way valve 24 , as well as through a heat exchange medium return circuit 52 connected to those jacket spaces 34 back into the inlet of the recirculation pump 34 . a feed line 55 with a stop valve 56 is provided for feeding or discharging the heat exchange medium . a heating and cooling device 58 is provided in the heat exchange medium feed line 46 , and heat exchange medium temperature sensors 60 and 62 are arranged upstream of the recirculating pump 44 and downstream of the heating and cooling device 58 , respectively , which sensors are connected via conduits 64 and 66 , respectively , to a central control unit 68 . the latter controls the heating and cooling device 58 via a connection 70 so that the temperature of the heat exchange medium is controlled in acordance with a predetermined program . the heating and cooling device 58 is not described here at greater detail , it being noted that this device may comprise for instance two heat exchangers which are supplied with hot and cold water , respectively , and are controlled by means of control valves . in addition to the measuring probe 20 already mentioned , further measuring and monitoring means may be provided , as particularly a level sensor ( not illustrated ) for sensing the filling level of the mass 4 in the vessel 2 , and a separate temperature sensor 72 which is also connected to the central control unit 68 via a connection 74 . furthermore , there will be normally display devices ( not illustrated ) provided for the temperature of the mass , the temperature of the heat exchange medium and other values of state . for instance , a typical tempering process can proceed in the tempering device illustrated in fig1 by the aid of the central control unit 68 as follows : at the beginning of the tempering process , the mass 4 is heated by means of the correspondingly heated heat exchange medium to a constant temperature of approximately 50 ° c , and the mass is continuously recirculated at that temperature by means of the mass pump 26 . the temperature of the heat exchange medium is also 50 ° c . in that condition , the mass temperature is above the melting point of the highest - melting cocoa butter crystal modification so that the mass does not contain any cocoa butter crystals . that molten mass which is held homogeneous by the recirculation is then cooled by first cooling the recirculating heat exchange medium relatively rapidly , e . g . within half an hour , to an intermediate temperature which is not too low , e . g . to approximately 33 ° c . in that first cooling stage , the mass is cooled down with a corresponding delay . the temperature of the mass is communicated to the central control unit 68 , e . g . from the temperature sensor 72 . as soon as the mass has attained the desired intermediate temperature , which for instance may be the case after approximately two hours , the temperature of the heat exchange medium is further lowered to approximately 26 ° c ., and the mass correspondingly cools down further in a second cooling stage . as soon as the mass has attained a definite second temperature , the heat exchange medium is heated to about 34 ° c ., and the temperature of the mass will follow until finally the mass reaches a constant third temperature of also approximately 34 ° c . ; at that temperature , the mass is ready for further processing and can be taken from the discharge conduit 42 . as the second temperature of the mass at which switching to the heating towards the third temperature is effected , the temperature is chosen at which a heat production is observed in the mass , which is due to undesired crystallisation processes . the reduction of the cooling rate of the mass , which is caused thereby , is sensed and measured and transferred into a switching order which initiates the heating towards the third temperature . fig2 shows strictly schematical in a temperature - time graph a cooling curve for the mass , it being assumed that the ordinate corresponds to the temperature . initially , there results a normal exponential cooling curve 76 . without the occurrence of heat - producing processes , that curve would continue according to the dashed line 78 . by the occurrence of a heat production , however , the cooling will be slowed down so that at a certain time t 2 , the cooling rate or cooling velocity will be only a predetermined fraction of the cooling rate which normally would have to be expected at that time . as a consequence of the heat production , the temperature of the mass does not follow the dashed line 78 but , rather , the line 80 . it is assumed in fig2 that the cooling capacity is relatively low so that the cooling rate of the mass can drop due to the initiation of the heat production to approximately zero . however , already at an earlier time , i . e . at the said time t 2 at which the mass has the temperature t 2 , the cooling process is terminated by switching on into the heating towards the third or processing temperature . fig3 shows in a similar representation as fig2 a typical course of the temperature of the mass in the case of a two - stage cooling . at the time t z , the temperature of the water which here serves as the heat exchange medium is rapidly lowered , and the still higher mass temperature follows correspondingly and approximates exponentially the new lower water temperature . the cooling curve of the mass , however , finally does not take the dashed course 78 but the course 80 caused by the self - heating so that again at a time t 2 at which the mass has the temperature t 2 , the cooling rate of the mass will be strongly reduced ; as soon as that reduction is present , the process is switched on to the heating towards the third temperature . fig4 illustrates the principal possibility to obtain a switching order for terminating the cooling from a measurement of the mass temperature . from a probe body 20 immersed into the mass , a temperature signal is delivered to a first amplifier v 1 via a connecting conduit 82 . in the probe body 20 , a transducer is provided , e . g . a thermo couple , a thermo battery or a resistance thermometer . the first amplifier v 1 delivers a correspondingly amplified electrical output signal to a differentiating stage d 1 which in known manner contains as effective components a rc combination consisting of a condenser c 1 and a resistor r 1 . the differentiating stage d 1 supplies to an intermediate amplifier v 2 a signal which is proportional to the first derivative with respect to time of the temperature of the mass . the output signal of the intermediate amplifier v 2 is again differentiated in a second differentiating stage d 2 which contains as effective components a condenser c 2 and a resistor r 2 , and the output signal which thus corresponds to the second timely derivative of the temperature of the mass , is supplied to a switching stage s 1 via a switching amplifier v 3 . in the entrance of the switching amplifier , a signal will appear only if the rate of change of the mass temperature changes , and the appearance of such a signal triggers in the switching stage s 1 a switching process by which the central control unit 68 ( see fig1 ) is caused to increase the temperature of the heat exchange medium and thus initiates the heating of the mass towards the third or processing temperature . fig5 illustrates a simplified possibility wherein the second differentiating stage d 2 is eliminated . in that case , the switching amplifier v 3 or the switching stage s 1 must have a discriminating effect , i . e . must trigger the desired switching process at a certain level of the output signal coming from the differentiating stage d 1 . for example , a schmitt trigger can be used for that purpose . such a device , however , can also be disposed of if for example the switching stage s 1 is provided with a relay which simply drops and thereby triggers the switching process when the exitation current for that relay as delivered from the output of the switching amplifier v 3 falls below a certain value . fig6 illustrates a possible embodiment with a digital evaluating device . in that case , the electrical temperature signal delivered from the probe body 20 via the connecting line 82 is transposed in an entrance stage 86 into a digital signal , and the digital signal is under control of a cycling unit 84 periodically , e . g . every 15 seconds , fed into a store 88 and a delay device 90 . the delay device 90 effects a delay by one cycle period or a plurality of cycle periods . the outputs of the store 88 and the delay device 90 are periodically compared in a comparator 92 , and the digital differential signal appearing in the output of the comparator 92 controls a switching stage s 1 . fig7 illustrates in a somewhat more detailed block circuit diagram an evaluating circuit of the kind shown in fig5 . the probe body contains a resistance thermometer in form of a resistor r 3 . via the two - line connecting conduit 82 , the resistor r 3 is arranged in a bridge circuit the other branches of which are formed by resistors r 4 , r 5 , r 6 and r 7 . the resistor r 6 is an adjustable resistor and serves for adjusting the zero point . the bridge is fed with supply voltage via the terminals 94 and 96 . the measuring voltage taken from the bridge diagonal is connected , in accordance with the schematic illustration in fig5 to the input of a voltage amplifier v 1 the output of which is connected to the input of a switching amplifier v 3 via a differentiating stage d 1 consisting of the condenser c 1 and the resistor r 1 . the output of the switching amplifier is connected to the switching stage s 1 via a filter circuit consisting of the resistor r 8 and the condenser c 3 . the condenser c 1 of the differentiating stage d 1 can be short - circuited with a switch s 2 ; then a signal which directly corresponds to the temperature of the mass will appear at the output of the amplifier v 3 . the switch s 2 may also be used to make the evaluation circuit operative only after the mass has reached a temperature which is only slightly above an expected second temperature . this can be made also automatically , for instance by opening the switch s 2 by means of a relay controlled by the output of the switching amplifier v 3 when the said temperature slightly above the expected second temperature has been reached . re - setting of the switch s 2 into the closed position can be effected by the switching stage s 1 upon triggering thereof . fig8 illustrates a modified embodiment of the circuit according to fig7 in which the input of the switching amplifier v 3 can be biased with an adjustable basic voltage obtained from a voltage divider r 9 , r 10 ; thereby the switching point at which the switching stage s 1 is triggered may be varied . the sensitivity of the differentiating stage will be the larger the larger the time constant of the rc member will be . because of the slowness and low magnitude of the temperature changes sensed , it is to the purpose to select a time constant as large as possible ; a limitation results from the requirement that the response speed must not be too low . in usual tempering processes , a time constant in the order of magnitude of one minute is to the purpose . this can be obtained , for example , with a condenser of 6 μf and a resistor of 10 mohm . of course , also switching means can be provided , if necessary , in order to rapidly switch between different time constants by selecting different condensers c 1 and / or resistors r 1 . in all other respects , the dimensioning of a practically useful circuit according to fig7 will not be in any way difficult for a skilled artisan . for the amplifiers v 1 and v3 , commercial operation amplifiers may be used , the amplification factors of which will have to be selected in accordance with the switching powers required in the switching stage s 1 . for purpose of stabilization , negative feed back can be provided in the amplifiers ; circuit particulars of that kind are not illustrated in fig7 and 8 . the resistor r 3 may for instance take the form of a platinum resistance thermometer of 100 ohm ; in correspondence thereto , the remaining resistors of the bridge may have approximately the following values : r 5 = 100 ohm , r 4 = 100 ohm , r 6 = 50 ohm , r 7 = 100 ohm . the filter in the output of the switching amplifier v 3 can be dimensioned in various ways according to the kind of possible disturbing influences which are to be suppressed ; it being understood that the time constant of that filter should be small as compared with the time constant of the differentiating stage d 1 . if for instance the time constant of the differentiating stage d 1 is approximately one minute , one may select r 8 = 50 kohm and c 3 = 50 μf which corresponds to a time constant of 2 . 5 seconds . fig9 illustrates in a schematic block representation similar to fig4 and 5 the basic structure of an evaluating device in case that a sensing means is provided in the probe body 20 , which responds directly to the rate of change of the temperature of the mass , whereby already the primary signal fed into the connecting line 82 will directly correspond to the rate of change of the temperature . then , differentiating stages are not necessary , and it is principally sufficient to provide an amplifier v 1 and a subsequent switching stage s 1 to obtain the desired effects . fig1 to 13 illustrate various simple possibilities to obtain a signal which corresponds directly to the rate of change of the temperature of the mass . according to fig1 , two sensing bodies 98 and 100 are immersed into the mass 4 , which bodies consist of materials of different heat conductivity and comprise in both cases in the center a temperature sensing element which delivers an electrical temperature signal via a conduit 102 and 104 , respectively . because of the different heat conductivities of the materials of the two sensing bodies 98 , 100 , different time constants will result for the heat transport from the mass 4 to the temperature sensing elements , and the differential of the signals delivered via the lines 102 and 104 thus is a measure for the rate of change of the temperature of the mass 4 . a somewhat different possibility is illustrated in fig1 . there , sensing bodies 106 and 108 are provided which consist of the same material but have different masses . also in those sensing bodies , sensing elements are arranged which deliver electrical temperature signals via lines 110 and 112 , respectively , the difference of which is a measure for the rate of change of the temperature of the mass 4 . fig1 illustrates the possibility of use two sensing bodies 114 , 116 which have different surface to volume ratios ; also thereby , a difference of time constants is obtained . the structure according to fig1 is particularly effective . a probe body 20 has two sensing bodies 118 and 120 immersed into the mass 4 . the sensing body 118 is surrounded by a heat insulation 122 which forms a certain heat resistance between the mass 4 and the sensing body 118 . the sensing body 120 is directly immersed in the mass 4 . it is readily apparent that thereby a large difference of the time constants associated with the two sensing bodies can be obtained . in order to avoid disturbing influences due to local temperature differentials in the mass , it is recommendable to operate devices of the kind shown in fig1 to 13 so that both sensing bodies are in heat - conducting connection with the mass 4 in a common contacting area . fig1 and 15 show embodiments of that kind which moreover offer the advantage of a compact and smooth construction . according to fig1 , a probe body 20 which is fastened to a holder 124 is immersed in the mass 4 . that probe body contains a cup - like housing 126 of low heat - conductive material , particularly plastic as polyethylene or the like , which housing is sealingly closed by a metal lid 128 . that metal lid 128 is directly in contact with the mass 4 and forms a connection of good heat conductivity to a temperature sensor 130 which may be directly soldered to the lid 128 . a second temperature sensor 132 is attached to a second sensing body 134 which consists of a metal block and is separated from the housing 126 by spacers 131 of low heat conductivity , and a heat insulating material 133 . at its end face which is disposed on the left side in fig1 , the second sensing body 134 is pressed onto the first sensing body ( lid 128 ) with the interposition of a separating plate 136 ; rather , there can also be provided a rigid connection , particularly by means of an adhesive , between the sensing bodies 128 and 134 under interposition of the separating plate 136 . the two temperature sensors 130 and 132 are connected opposed to each other via a line 138 , whereby a signal corresponding to the temperature differential between the two sensing bodies 128 , 134 will be delivered via the two - line connecting conduit 140 . the connecting conduit 140 extends through a sealed screw terminal 142 from the housing 126 . it will be appreciated that in the device illustrated in fig1 , the temperature differential which is sensed between the two sensing bodies 128 and 134 will be a measure for the rate of change of the temperature of the mass 4 because the one sensing body ( lid ) 128 is directly in good heat - conducting connection with the mass 4 , whereas the second sensing body 134 is heat - insulated towards the mass 4 and thus is in heat exchange with the mass 4 substantially only via conduction through the separating plate 136 . both sensing bodies 128 and 134 are in heat - conducting connection with the mass via the same contacting area , namely the surface of the lid 128 which is shown in fig1 on the left side of the lid . it will be further appreciated that for devices of the kind shown in fig1 , it is particularly useful to employ thermo couples or thermo batteries as temperature sensors because those devices are inherently responsive to temperature differentials and are free of self - heating . since the heat resistance between the mass 4 and the one sensing body 128 is negligible as compared with the heat resistance between the mass 4 and the second sensing body 134 , the response characteristic of the device shown in fig1 will be substantially determined by the time constant of the heat - conducting connection to the second sensing body 134 . that time constant may be calculated with good approximation if it is assumed that the whole heat exchange with the second sensing body 134 takes place via the separating plate 136 only , the heat capacity of which is negligibly small as compared with that of the second sensing body 134 . on the other hand , the heat resistance is formed practically exclusively by the separating plate 136 . the time constant then is simply the product of the heat resistance of the separating plate 136 , taken acorss the contact cross - section with the second sensing body 134 , and the heat capacity of the second sensing body 134 . for instance , with a second sensing body 134 consisting of 10 grams of copper and having a cross - section of 1 cm 2 , which engages a separating plate 136 of polystyrene foil of 0 . 2 mm thickness , a time constant of approximately 0 . 8 minutes will result . in that case , the sensitivity will be approximately 0 . 8 minutes , i . e . the resulting temperature differential between the two sensing bodies 128 and 134 will be in the maximum approximately 0 . 8 ° c . per degree per minute temperature change of the mass 4 . fig1 illustrates a similar embodiment as fig1 . however , there is a further simplification provided in that a single unitary sensing body 144 only is used . that sensing body consists of a first area 146 which as in the embodiment of fig1 forms a lid of the housing 126 , a second area 148 spaced therefrom , which corresponds to the second sensing body 134 of the embodiment according to fig1 and is heat - insulated from the housing 126 as in that other embodiment by means of spacers 131 and heat - insulating material 133 , and a web - like connecting piece 150 which corresponds to the separating plates 136 of the embodiment according to fig1 and forms a heat - conducting connection between the areas 146 and 148 . as sensing elements , a plurality of thermo couples 149 are provided which are series - connected to form a thermo battery , whereby the signal voltage is correspondingly increased which is delivered via the connecting conduit 140 and which is proportional to the temperature differential between the areas 146 and 148 . fig1 shows at greater detail an evaluating circuit of the kind of the circuit shown in fig7 . instead of the single amplifier v 1 illustrated in fig7 the circuit according to fig1 comprises two series - connected operation amplifiers v 11 and v 12 . ahead of the switching amplifier v 3 , a voltage divider r 9 , r 10 for adjusting the basic voltage is provided as in fig8 . the individual amplifiers are stabilized by negative feed back , as by the negative feed back path including resistors r 12 and r 13 and condensor c 4 in the amplifier v 11 , and by resistors r 17 and r 18 and condenser c 5 in the amplifier v 3 . the bridge circuit is supplied via a series resistor r 16 with a stabilizing diode d 1 . the diagonal voltage is fed into the amplifier v 11 via a protective resistor r 11 . the amplifiers v 11 , v 12 and v 3 are commercial operational amplifiers . in other respects , possible values for the individual circuit components are indicated in fig1 , whereby a closer description of fig1 does not appear to be necessary .
a method and device of treatment of cocoa butter - containing masses , particularly molten chocolates , destined for subsequent processing , particularly in coating machines , the method comprising the steps of mildly cooling the mass from a first temperature of approximately 45 ° to 50 ° c . which is above the highest melting point of the mass to a second temperature at which pre - crystallization in the mass is initiated , sensing the occurrence of heat - producing processes in the mass during the cooling thereof , terminating the cooling upon the occurrence of such heat - producing processes , and thereafter mildly heating the mass , without overheating , to a third temperature of approximately 33 ° to 34 ° c ., at which the mass is ready for said subsequent processing . the second temperature is thus automatically adjusted to the lowest possible value , which is desirable for the processing properties of the mass .