HEAT CONSUMPTION METER

Abstract: Device for measuring the consumption of heat supplied by a fluid medium, consisting of one or more heat exchangers 10, 12 and a temperature differential meter 11, 13 connected in series. A side stream originating from the supply conduit 2 for the medium and a side stream originating from the return conduit 4 for the medium, or having the same temperature as the medium in the latter conduit 4, which streams are of equal size, are brought in counter current in heat exchange relation in the heat exchanger(s) 10, 12 and the temperature differen­ tial meter 11, 13. The electric output signal of the meter 11, 13 is proportional with the heat consumption to be measured.

Description: Heat consumption meter. The invention relates to a device for measuring the quantity of free heat instantaneously supplied to or withdrawn from an installation by a fluid medium, which installation is provided with a conduit for supplying the medium and with a conduit for withdrawing the medium, said device comprising a first heat exchanger the one channel of which forms part of a by-pass line connected to the one conduit and the other channel of which is coupled to the other conduit in such a manner that the medium flowing through this channel is at an entrance temperature equalling or substantially equalling the temperature of the medium in the other conduit and flows in a direction opposite to the direction of the flow in the said one channel, said device furthermore comprising means for temperature measuring. In technical practice it is frequently found desirable to determine the quantity of free heat supplied to of withdrawn from an installation by a fluid medium in the course of a period of time. As example of such installations there may be mentioned central heating installations to which hot water or a hot gas is supplied and cooling installations through which cooled brine or an other. refrigerated liquid is passed. The invention however does not relate to central heating installations operated on steam or cooling installations to which liquid ammonia is supplied because in such installations not only the ree heat but also the heat of condensation or the heat of evaporationrespectively, play an important role. Assuming that in installations with which the present invention is concerned the specific weight and the specific heat of the medium in the supply conduit equal those in the return conduit the instantaneous positive or negative thermal energy consumption of an installation may be determined from the difference in temperature of the medium in the supply conduit and in the return conduit and the flow rate of the medium in the spply conduit or the return conduit. The instantaneous positive or negative heat consumption, respectively, equals the product of the difference in iamperature measured, the flow rate, the density an the specific heat of the medium. The total consumption over a period of time is determined by integrating the instantaneous consumption over this period of time in a way known per se. For purposes of illustration the invention will be elucidated herein-after only with respect to heat consumption, i.e. a positive heat consumption, though it will be clear that the same applies to a negative heat consumption so that the following disclosure also applies to for instance installations refrigerated by means of a cooled brine. For a long time already research has been directed to devices for measuring the instantaneous heat consumption in which such consumption is not determined by the product of a separately measured temperature differential and flow rate but is derived from one single measured quantity. The German Patent Specifications - Nos. 356,313 and 389,380 each relate to a device for measuring the instantaneous heat consumption in which a flow of medium in a by-pass line connected to the supply conduit of an installation is brought into heat exchanging relation cross current wise with the medium in the return conduit, while measuring the difference between the temperature of the medium in the by-pass line or upon leaving the heat exchanger, respectively, and the temperature of the medium in the return conduit by means of thermo-couples. The German Patent specification numer 389,380 states that the temperature differential thus measured and consequently also the output signal of the thermal-couples is proportional to the instantaneous heat consumption. This, however, is not correct: the measured temperature differential, it is true, is proportional to the difference between the temperature of the medium in the supply conduit and that of the medium in the return conduit, though to ane-power of the flow rate. Only within a very narrow range of the flow rate and with a very coarse approximation this e-power of the flow rate may be assumed to be a linear relation. The above described device is known from the Dutch Patent Specification No. 11,208. In the device disclosed in this patent specification a by-pass line 2 is connected to a supply conduit 4 supplying a hot medium to a heating installation. The medium flowing through this by-pass line 2 is brought into heat exchanging relation with the whole return flow in the conduit 3. From the temperatures indicated in the figure it may be calculated that the size of the flow through the return conduit 3 and of that through the by-pass line 2 are in a ratio of 25:1. Although this patent specification only gives a detailed description of the case in which the two flows of medium through the heat exchanger flow in the same direction (parallel current heat exchanger) and the temperatures indicated in the figure also only relate to this case the possibility of counter current has nevertheless been mentioned (page 1, right hand column, lines 89-92). A drawback of the device described in the above mentioned Dutch Patent specification is however thattheheat exchanger and the thermo-couples combined to a thermo-pile are constructed as a single assembly. The heat conductivity per unit of area of such an assembly is relatively low for that matter so that a large surface area will become necessary. Whore in case of heat exchange in parallel current the thermo-pile has an integrating function it will not be possible to design the heat exchanger and the thermo-pile as separate units arranged in series. The present invention is now based on the conception that upon heat exchange in counter current and correctly dimensioning the device the temperature difference between the two flows of medium only needs to be measuredatone single location and that the heat exchanger and the measuring means may therefore be designed as eeparate units.Such a design entails the advantage that the heat exchanger may be of a type having a high coefficient of heat transmission whereby the required heat exchanging area may be small. The invention therefore relates to a device of the above described type said device being characirized in that outside the heat exchanger there is provided a measuring means for measuring the difference between the temperature of the flow entering the heat exchanger and the temperature of the flow leaving the heat exchanger at the same location and that the device is designed in such a manner that the two flows passing through said first heat exchanger are at any rate substantially alike. This is in contrast with the device described in the Dutch Patent Specification 11,208 in which the sizes of the two flows are in a ratio of 25:1. It may be achieved that two flows of medium of about equal size will pass through the heat exchanger by incorporating the one channel of the heat exchanger ina by-pass line connected to the supply conduit of the installation while the other channel of the heat exchanger is incorporated in aby-pass line connected to the return conduit. In this connection it should be remarked that the French Patent Specification No. 806,033 describes a device for measuring the instantaneous heat consumption said device including a heat exchanger the one flow channel of which is also incorporated in a by-pass line connected to the supply conduit whereas the other flow channel of this heat exchanger is incorporated in a bypass line connected to the return conduit. This heat exchanger has, however, been combined with an integrating thermo-pile. This is necessary because in accordance with this French Patent Specification the two flows of medium havethe same direction in the exchanger (vide Figs. 1, 2, 3 and 7). In Pigs. 9 and following the flows of medium in the two by-pass lines (4 and 5 in Fig. 9) are, it is true, in the same direction but in this case there is not at stake any direct heat exchange between these two flows but rather a heat exchange between each one of these flows and the flow of another medium for instance air. In accordance with a preferred embodiment of the invention it is achieved that the sizes of the flows in the two channels of the first heat exchanger are complete alike by arranging these two channels in series. Between these two channels however the first channel of a second heat exchanger is arranged in series. The second channel of this second heat exchanger forms part of ( a by-pass line connected to) the other conduit. Furthermore it is preferred that the measuring means comprises one or a plurality of thermo-couples arranged in series electrically (thermo-pile). The invention will now be described with reference to the drawings, in which Fig. 1 diagrammatically shows how the heat consumption of an installation may be determined, Fig. 2 represents a first embodiment of a device according to the invention, Fig. 3 represents a second embodiment of a device according to the invention; Fig. 4 shows the course of the temperature in a device according to Fig. 2, Fig. 5 shows the course of the temperature in a device according to Fig. 3, Fig. 6 shows an embodiment of a heat exchanger for use in a device according to the invention, Fig. 7 represents an embodiment of the device according to the invention having a thermal screen. Fig. 8 represents the course of the temperature in the device of Fig. 7, Fig. 9 shows a variation of the device according to the invention as shown in Fig. 3, Fig. 10 shows a modification of the device according to the invention as shown in Fig. 9, Fig. 11 represents a perspective side elevation partially cut away of a device according to the invention, and Fig. 12 shows a diagram representing the relation between the output potential of a thermo-pile and the flow rate in the device of Fig. 11. With reference to Fig. 1 there is shown diagrammatically a source of heat 1 heating a liquid medium. By way of a supply conduit 2 the heated medium at a temperature TH and a flow rate 0 is supplied to a heat consuming installation 3. The medium cooled down to a temperature Tij in this installation 3 is returned by way of a return conduit 4 to the source of heat 1. The supplied flow of medium as well as the return flow are passed through a consumption meter 5 emitting an electric signal V which signal is proportional to the instantaneous heat consumption. V = K.. 9 .c (TH- E ) This electric signal V is transmitted to an integrator 6 integrating the potential V over a period between the point of time t1 and t2. The integral EMI6.1 indicates the total consumption within the said period and may for instance be read on a display device 7. With reference to Fig. 2 there is shown the heat consumption meter indicated diagrammatically at 5 in Fig. 1 in a more detailed manner. The supply conduit 2 includes a constriction 8. By-passing the constriction 8 there is provided a by-pass line comprising (1 among others the channel 10 of a heat exchanger 25 and the channel of a temperature differential meter 26. This by-pass line includes furthermore a constriction 14. By-passing the constriction 9 there is provided a by-pass line comprising among others a channel 12 of the said heat exchanger and the channel 13 of the said temperature differential meter. This by-pass line furthermore includes a constriction 15. The constrictions and the by-pass lines have been dimensioned such that at a varying flow rate of the medium the ratio between the sizes of the flow in the supply conduit and the return conduit, respectively, and that of the flows in the associated by-pass lines, is constant. The said constrictions and by-pass lines have furthermore been dimensioned such that the flows in the two by-pass lines are at any rate approximately equal. Fig. 4 shows the course of the temperature of the medium in the two by-pass lines of the device shown in Fig. 2, for that matter as a function of the flow path x in the respective by-pass lines. From this figure it is apparent that along the entire flow path the difference between the temperatures of the flows of the medium in the two by-pass lines is substantially constant. It will be demonstrated below that this temperature difference is a measure ior the heat consumption to be measured. Where it will not be easy to construct the device according to Fig. 2 in such a manner that the flows in the two by-pass lines will be substantially equal at any flow rate there have been designed a variation shown in Fig. 3 of the device according to Fig. 2 in which the two channels 10 and 12 of the heat exchanger are arranged in series thus assuring that the flows through these two channels will always be equal. Between the channels 10 and 11 of the heat exchanger 25 arranged in series and the associated channels 11 and 13 of the temperature differential meter 26 there is arranged a second heat exchanger or return heat exchanger 16 in which the flow of medium leaving the channels 10 and 11 are brought into heat exchanging relation with the medium in the return conduit 4. In stead of within the return conduit 4 per se there may be also be provided the heat exchanger 16 in a by-pass line connected to the return conduit. With reference to Fig. 5 there is shown the course of the temperature of the flow of medium through the device shown in Fig. 3, for that matter as a function of the flow path x. In order to facilitate a comparison with Fig. 4 the flow path downstream of the second (return) heat exchanger has been plotted in the inverse direction. If heat losses to the surroundings and conduction in longitudinal direction within the heat exchanger are not taken into consideration, the following relations will hold for the device shown in Fig. 3: q = a .y .dT (1) qws = &alpha;ws#Fws#dT (2) qw = k#####c##Tw (3) qws = kk#####c##Tws (4) TL 2- TL1 =1-e-p (5) TL2 - TL in which: R#Fr p=k#####c (6) From these relations there may be derived: EMI8.1 in which: k#####.c z = (8) &alpha;w#Fw+&alpha;ws#Fws By selecting p and z such that: 1 # z < < 1 (9) 1-e-P relation (7) changes into: EMI8.2 qws = K1#####c(TH-TL) (11) or by combining relation (11) with relation (2) dT = K2#####c(TH-TL) (12) The temperature difference dT measured by the temperature differential meter is thus proportional to the instantaneous heat consumption provided the requirement of relation (9) is met. The term 1 in (6) is always larger than 1. When selecting 1-e-P for instance p = 5, 1 1-e P so that there will then yet remain as a requirement z < < 1 (13). The requirements stated for p and z may be met for instance by adjusting the constrictions to a value of k which is in agreement with the range of the flow rate to be expected. At z < < 1 there applies z = dT TH-TL Stated otherwise dT amounts to only a fraction of the difference between the supply temperature and the return temperature of the medium. A practical solution may then for instance be the use of a thermo-pile in order to make a sufficient measuring signal available nevertheless. The result will then be: V=K3.. p .c(T-TL) (14) The relations applying to the device shown in Fig. 2 may be found by substituting in the relations derived for the device according to Fig. 3: L1 Tb (15) whereby (5) changes into = P = 1 (16) The relations (12), (13) and (14) apply also for the device shown in Fig. 2. The requirement indicated in (9) is however simplified to the requirement of (13). It has been remarked above that the above derived relations only apply if it is assumed among others that nn transmission of heat in the longitudinal direction occurs within the heat exchanger. With reference to Fig. 6 there is shown diagrammatically a heat exchanger in which the transmission of heat in the longitudinal direction is reduced to a minimum. This heat exchanger consists of a box divided into two approximately equal spaces by means of a foil consisting of a material having a good heat conductivity. For enlarging the surface area of the foil it is preferred to provide the foil with a number of parallel foils shirred like the bellows of an accordion. Each one of the two spaces into which the box has been divided is provided with an inlet and an outlet, that is to say in such a manner that the flow in the one space will be in the opposite direction with respect to the flow in the other space. The upper space has an inlet 20 and an outlet 21 whereas the lower space separated by means of the foil 22 from the upper space has an inlet 23 and an outlet not shown in the drawing but present at the left hand side in the rear. It is also possible to restrict the conduction of heat in the longitudinal direction within the heat exchanger by building the heat exchanger of a plurality of approximately similar elements which elements are arranged consecutively in the direction of the flow and consists alternating of a thermally well conducting material and of a thermally badly conducting material, respectively, or by applying a known heat exchanger comprising a plurality of foils stacked onto each other between which foils there are spaces through which alternatingly the one and the other flowing medium will flow. Furthermore it has been assumed above that no heat exchange will occur with respect to the surroundings. In practice, however, heat will dissipate with certainty to the surroundings and even at an increasing rate if the difference between the mean temperature pf a flow of medium in the device and the temperature of itle surroundings To becomes larger. The exchange of heat with the surroundings may be restricted by enclosing the device according to the invention with an insulating material while it is furthermore very effective to enclose the device by a shell the temperature of which at any location substantially equals the mean of the temperatures of the flows of medium present at that location within said shell. Such a shell may be obtained by enclosing the device according to the invention with an envelope of thermally well conductive materialtbethickness of which is reciprocally proportional to the temperature radiant to be expected of the mean of the temperatures of the flows of medium present at that location witin the shell, which shell furthermore atthe one extremity thereof is arranged in good thermal contact with the supply conduit and at the other extremity thereof with the return conduit. Such a shell manufactured of copper for instance and indicated in Fig. 7 at 24 encloses the device 5 according to the invention and is in good thermal contact with both the supply conduit 2 and with the return conduit 4 for the medium. The shell 24 as well as the device 5 are completely embedded within an insulating material ( indicated by the speckled surface). With reference to Fig. 8 there is shown the temperature profile of the device shown in Fig. 7. The two obliquely running un- inter,rupted lines indicate the temperatures within the two branches of the device 5 shown in Fig. 7 whereas the dash line indicates the temperature of the shell 24 shown in Fig. 7. It will be appreciated that the temperature of the shell coincides almost everywhere with those of the flows of medium so that there will be substantially no heat exchange between the shell and these flows. In the device shown in Fig. 3 the by-pass line is connected to the supply conduit for the medium whereas the second (return) heat exchanger is in thermal contact with the return conduit for the medium. This device may however also be designed in the inverse manner, that is to say such that the by-pass line is connected to the return conduit for the medium and that the second heat exchanger is in thermal contact with the supply conduit for the medium. Furthermore the order indicated in Figs. 2 and 3 of the first heat exchanger 25 and the temperature differential meter 26 may be reversed in such a manner that the partial flow of the medium derived from the supply conduit first passes through the temperature differential meter 26 and only thereafter through the first heat exchanger 25. Such a variation of the device shown in Fig. 3 has been represented in Fig. 9 in which the order of the heat exchanger and the temperature differential meter has been inversed. Finally it is also possible to built a first heat exchanger 25 not only of a plurality of partial heat exchangers 25', 25" arranged in series but also to insert the temperature differential meter 26 between two of these partial heat exchangers. Fig. 10 shows diagrammatically how such may be realized in the device shown in Fig. 3. In this case the heat differential meter 26 is accommodated between two partial heat exchangers 25' and 25". With reference to Fig. 11 there is shown a perspective side elevation partially cut away of a device according to the invention made in accordance with the design of Fig. 10 and dest ined for measuring the instantaneous heat consumption of an installation operated on hot water. Hot water at a temperature TH is supplied to an installation ( not shown in the drawing) by way of the conduit 2. Slightly cooled water at a temperature TL is returned by way of the return conduit 4. In the conduit 2 there is provided an interchangeable flange having a constriction 8. Upstream and downstream of this flange a by-pass line is connected to the conduit 2 in which bypass line there has been accommodated a flange having a constriction 14. Water in this by-pass line flows by way of the braching provided in the drawing on the right hand side of the constriction 8 through the two partial heat exchangers 25 and ibe temperature differential meter 26/while entering thereupon the second (return) heat exchanger 16 in which heat exchange occurs with the water flowing through the return conduit 4, then passing through the partial heat exchangers 25 and the tpera- ture differential meter 26 in the reverse order and finally arriving again in the conduit 2 through the branching shown at the left hand side of the constriction 8 in the drawing. In the temperature differential meter 26 there is provided a thermo-pile. At 27 there may be seen part of the lamellae constituting the heat exchangers 25. The device shown in Pig. 11 the height of which amounts to about 20 cm is completely enclosed by a thermally insulating material and accommodated together with this material in a copper box 24. This copper box 24 is arranged in good thermal contact with the conduits 2 and 4. The thickness of the bottom of the box is considerably larger than that of the side walls. The diagram of Fig. 12 relates to measurements performed with the device shown in Fig. 11. Along the vertical axis there is plotted the output potential (V in mV) of the thermo-pile in the temperature differential meter 26 and on the horizontal axis there is plaited the amount of water flowing through the heat exchangers per unit of time (k# in cmê/sec). During the measurement Tand TL were kept constant at 50 C and 20 CErespectively. The ambient temperature also amounted to 20q. Prom the diagram it is apparent that there is a substantially linear relation between V and k. 7arranged in between List of symbols used. &alpha;w coefficient of heat transmission of the heat exchanger [W/mê#K] a coefficient of heat transmission of the temperature ws 2 differential meter [W/m K] a coefficient of heat transmission of the second (return) r heat exchager [W/m2 K] heat exchanger [W/mê#K] c specific heat of medium [J/kg.K] dT temperature difference between the primary and second arty part of the first heat exchanger and in the tempe rature differential meter [Pc] e base of the Napierian logarithm F heat exchanging area of the first heat exchanger [mê] w F heat exchanging area of the temperature differential me ws 2 ter [m ] F heat exchanging area of the second (return) heat exchan r ger [m2] K proportion constant K1 proportion constant K2 proportion constant K3 proportion constant k fraction of # in the by-pass line ar F r k.0.? .c qw heat exchanged by the first heat exchanger [W] heat exchanged by the temperature differential meter [W] heat exchanged by the second (return) heat exchanger [W] r second (return) heat exchanger TH temperature of the supplied medium [K] TL temperature of the return medium [K] TL1 temperature of the medium at the exit of the second (return) heat exchanger UK] T temperature of the medium at the entrance of the second L2 (return) heat exchanger [K] <RTI ID=14.1> ATw fall (raise) in temperature in the primary (secondary) side of the first heat exchanger (w) [ C] #Tws fall (raise) in temperature in the primary (secondary) side of the temperature differential meter (ws) [ C J ti point of time of commencement of measuring the heat con sumption t2 point of time of the end of measurement of the heat con sumption V electric signal transmitted by the thermo-pile [mV] ws temperature differential meter w first heat exchanger xn location coordinate in the temperature profile curve corresponding with a location in the heat consumption meter z k#####c &alpha;w#Fw+&alpha;ws#Fws flow rate of the medium in the heating circuit [m3/sec] density of the medium [kg/m3]

Claims: C b A I N S. 1. A device for measuring the quantity of free heat instantaneously supplied to or withdrawn from an installation by a fluid medium which installation is provided with a conduit for supplying the medium and with a conduit for withdrawing the medium, the said device comprising a (first) heat exchanger the one channel of which forms part of a by-pass line connected to the one conduit and the other channel of which is coupled to the other conduit in such a manner that the medium flowing through this channel is at an entrance temperature equalling or substantially equalling the temperature of the medium in the other conduit and flows in a direction opposite to the direction of the flow in the said one channel, said device furthermore comprising means for temperature measuring c h a r a c t e r i z e d i n t h a t outside the heat exchanger there is provided a measuring means for measuring the difference between the temperature of the flow entering the heat exchanger and the temperature of the flow leaving the heat exchanger at the same location and that the device is designed in such a manner that the two flows passing through said (first) heat exchanger are at any rate substantially alike. 2. The device according to claim 1 c h a r a c t e r i z e d i n t h a t the other channel of said (first) heat exchanger forms part of a by-pass line connected to the other conduit. 3. The device according to claim 1 c h a r a c t e r i z e d i n t h a t the two channels are arranged in series with each other and with the first channel of a second heat exchanger, the first channel of said second heat exchanger being located between the two channels of said first heat exchanger while the second channel of said second heat exchanger forms part of ( a by-pass line connected to ) the other conduit. 4. The device according to anyone of the preceding claims c h a r a c t e r i z e d i n t h a t the measuring means comprises one or a plurality of thermo-couplesarranged in series electrically ( thermo-pile). 5. The device according to anyone of the preceding claims c h a r a c t e r i z e d i n t h a t the first heat exchanger consists of one or more pairs of approximately equal spaces which spaces of each pair are separated from each other by a foil having a low thermal resistance. 6. The device according to claim 5 c h a r a c t e r i z ed i n t h a t the foil is provided with a number of parallel folds shirred like the bellows of an accordion. 7. The device according to anyone of claims 1-4, c h a r a ct e r i z e d i n t h a t said first heat exchanger consists of a plurality of elements arranged consecutively in the direction of the flow in one of the channels, said elements alternatingly being made of a thermally well conducting material and of a thermally insulating material, respectively. 8. The device according to anyone of the preceding claims char a c t e r i z e d i n that the device including its inlet and outlet tubes is thermally insulated with respect to the surroundings. 9. The device according to anyone of the preceding claims c h a r a c t e r i z e d i n t h a t the device and its inlet and outlet tubes are enclosed by a shell designed in such a manner that at each location the temperature of said shell may be made to equal the,mean of the temperatures of the flows of medium present at the said location within said shell. 10. The device according to claim 9 c h a r a c t e r i zed i n t h a t the shell consists of thermally well conductive material the thickness at any location of which is reciprocally proportional to the temperature gradient to be expected of the mean of the temperatures of the flows of medium present at that location within the shell, said shell at the one extremity thereof being arranged in good thermal contact with the one conduit and at the other extremity thereof in good thermal contact with the other conduit. 11. A method for measuring the quantity of free heat instantaneously supplied to or withdrawn from an installation by a fluid medium while applying a device according to-claim 1 and 2 and optionally one or more of the claims 4-10, whereby the difference in temperature measured by said measuring means is approximate ly proportional to the quantity of heat to be measured c h a r a c t e r i z e d i n t h a t the device is operated in such a manner that k#####c z= < < 1 &alpha;w#Fw+&alpha;ws#Fws wherein: : = the quantity of medium flowing through the installation per unit of time (m3/sec), k = the fraction of ej flowing through one of the channels of the heat exchanger; p = the density of the medium (kg/m3), c = the specific heat of the medium ( J/kg.K), a = the coefficient of heat transmission of the (first) heat w 2 exchanger (W/m .K), a = the coefficient of heat transmission of the measuring ws means (W/m K), 2 F = the heat exchanging area of the (first) heat exchanger (m2), w the 2 F = the heat exchanging area of the measuring means (m ) ws 12. A method for measuring the quantity of free heat instan taneously supplied to or withdrawn from an installation by fluid medium while applying a device according to claims 1 and 3 and optionally one or more of the claims 4-10, whereby the difference in temperature measured by the measuring means is appoximately proportional to the quantity of heat to be measured c h a r a c t e r i z e d i n t h a t the device is operated in such a manner that 1 . An 1 1 - e-P wherein z = the quantity defined in claim 11, e = the base number of the Napierian logarithm, &alpha;r#Fr P= , k#####c wherein &alpha; ;r = the coefficient of heat transmission of the second (return) heat exchanger, Fr = the heat exchanging area of the second (return) heat ex change, and and #,# and c are as defined in claim 11.

Inventors: GRAAF VAN DER, FREDERIK
Applicants: NEDERLANDSE CENTRALE ORGANISATIE VOOR TOEGEPAST-NATUURWETENSCHAPPELIJK ONDERZOEK
Application year: 1980
Main classification: G01K17
IPC codes: G01K17