CA1172872A - Groundwater flow meter - Google Patents
Groundwater flow meterInfo
- Publication number
- CA1172872A CA1172872A CA000380663A CA380663A CA1172872A CA 1172872 A CA1172872 A CA 1172872A CA 000380663 A CA000380663 A CA 000380663A CA 380663 A CA380663 A CA 380663A CA 1172872 A CA1172872 A CA 1172872A
- Authority
- CA
- Canada
- Prior art keywords
- fluid
- flow
- sensors
- medium
- temperature
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01P—MEASURING LINEAR OR ANGULAR SPEED, ACCELERATION, DECELERATION, OR SHOCK; INDICATING PRESENCE, ABSENCE, OR DIRECTION, OF MOVEMENT
- G01P13/00—Indicating or recording presence, absence, or direction, of movement
- G01P13/0006—Indicating or recording presence, absence, or direction, of movement of fluids or of granulous or powder-like substances
- G01P13/006—Indicating or recording presence, absence, or direction, of movement of fluids or of granulous or powder-like substances by using thermal variables
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01P—MEASURING LINEAR OR ANGULAR SPEED, ACCELERATION, DECELERATION, OR SHOCK; INDICATING PRESENCE, ABSENCE, OR DIRECTION, OF MOVEMENT
- G01P5/00—Measuring speed of fluids, e.g. of air stream; Measuring speed of bodies relative to fluids, e.g. of ship, of aircraft
- G01P5/10—Measuring speed of fluids, e.g. of air stream; Measuring speed of bodies relative to fluids, e.g. of ship, of aircraft by measuring thermal variables
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- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Engineering & Computer Science (AREA)
- Aviation & Aerospace Engineering (AREA)
- Geophysics And Detection Of Objects (AREA)
- Indicating Or Recording The Presence, Absence, Or Direction Of Movement (AREA)
- Sampling And Sample Adjustment (AREA)
- Investigating Or Analysing Biological Materials (AREA)
- Investigating Or Analyzing Materials Using Thermal Means (AREA)
Abstract
ABSTRACT OF THE DISCLOSURE
Flow characteristics of a fluid through a permeable solid medium are determined by introducing a predetermined quantity of thermal energy at a highly localized point within the medium and subsequently mapping temperatures around such point to determine the direction and rate of fluid flow through the medium.
Flow characteristics of a fluid through a permeable solid medium are determined by introducing a predetermined quantity of thermal energy at a highly localized point within the medium and subsequently mapping temperatures around such point to determine the direction and rate of fluid flow through the medium.
Description
-
2~7~
~ lthouyh this invention is directed principally to the measurement of direction and/or rate of groundwater flow in order to determi.ne the environmental effect, for example, of septic leachate upon natural water systems, the basic principles of this invention are applicable to a wide range of problems in which the velocity and/or direction of fluid flow is in question.
At present, many systems and techniques have been developed to provide information about the direction and/or rate of a fluid flow, including systems which rely on steady state heating a tube through which a liquid flows and measuring temperatures of the moving li~uid at upstream and downstream locations relative to the heat source, to obtain a hyperbolic measurement of flow rate. However, none has to my knowledge been developed which involves measurement of the distortion of a thermal field established by locally heating a permeable mass through which the f].uid flows, to obtain a linear measurement of fluid flow rate.
rrhis invent.ion relates to the discovery that the distortion of a thermal field established in a porous medium through which a very slowly flowing groundwater system moves, can be used to provide a linear measurement of the rate of such groundwater flow. ~ore specifically, it was found that if temperature measurements are made at different regions of the distorted field, so as in effect to "map" it, not only can the flow azimuth be determined, but also the rate of flow can be determined.
In a basic arrangement, the thermal field is established by transferring a predetermined quantity of heat energy to a highly localized region of a porous heat ~72~7'~
conductive medium through which the groundwater flows.
The localized region is at -the center o~ a surrounding array of ternperature sensors. By not.ing the temperature change differential between diametrically opposed pairs of sensors, the pair indicating the greatest such differ-ential provides information concerning the direction of flow whereas the amplitude o~ the differential provides a linear indication of the rate of flow.
In such system, the heat source was "pulsed"
whereafter the maximum temperature differentials between the pairs of the sensors were recorded. It was discovered that over a wide ran~e of groundwater flow velocities, the temperature differentials peaked after the same elapsed time subsequent to cessation of the heat "pulse", and that the variation in maximum temperature differential in the direction of flow, was essentially linearly related to groundwater flow rate of velocity.
Figure 1 is a schematic diagram illustrating certain basic features of the invention, Figure 2 is a graph illustrating the li~earity between maximum temperature differential and fluid flow rate, Figure 3 is a schematic illustrating one embodiment of the invention, Figure 4 is a schematic view illustrating one embodiment of a proble assembly and associated measuring circuitry, Figure 5 is a graph illustrating certain properties of the invention, and 2~
Figure 6 is a circuit diagram showing a modified form of the control assembly Referring more particularly to Figure 1, certair.
principles of the present invention will be apparent therefrom. As illustrated, a pair of temperature sensing means 10 and 12 and which in the specific construction illustrated take the form of termistors, are arrayed on opposite sides of a heating element indicated generally by the reference character 14. It will be understood that the sensing means 10 and 12 as well as the heater 14 are to be disposed within a porous heat conductive medium M through which the fluid whose flow character-istics are being measured, flows. In the groundwater system, the porous medium can be the soil itself, in which case the naked heater and sensor may be inserted thereinto. However, the sensing means and the heater are preferably embedded in a porous or permeable mass to provide a probe element to assure uniform and accurate heat conductivity. When such an arrangement is used, the porous mass should be formed of substantially uni-formly sized spherical particles having heat conductivity substantially greater than that of the fluid whose flow is being measured, the particle size being not greater than about 1.0 mm in diameter and sufficiently large as will not impede, distort or adversely affect the normal groundwater flow.
~'7ZB7~
In any even, with the arrangement as shown, a timer indicated generally by the reference character 16 is actuated by suitable means not illustrated to energize the heater 14 from the power source 18 for a predeter-mined period of time In this way, a predetermined quantity of thermal energy is introduced, the ammeter 20 being illustrated in the line connection to the heater 14 to illustrate this fact, i.e~, that the arrangement is such as to provide a control power input to the heater 14 such that the heater dissipates a predetermined quantity of heat conductive medium during a predetermined period of time controlled by the timer 16.
In this fashion, the heater 14 is "pulsed" to heat the porous mass M and establish a thermal field within the flow path of the fluid whose flow character-istics are being measured. In the absence of fluid flow or movement, the field is centered about the location of the heater 14 and is symmetrical or of predetermined shape with respect thereto.
The two thermistors 10 and 12 are connected to a suitable source 22 and the two branches of the circuitry to the individual sensors 10 and 12 include, in addition to the variable resistance displayed by the sensors, the resistors 2~ and 26 respectively and a common variable resistance element 28 suitably grounded as shown to ~L~72~7~
connect the opposite side of the supply 22. The two resistors 24 and 26 are o~ equal value and the resistor 28 is variable to establish a calibrated set point or zero at the volt meter 30 at some predetermined temper-ature of the two thermistors 10 and 12 The aforementioned thermal field, in the presence of fluid movement or flow, will be distorted and the deviation represented thereby will, dependent upon the direction of flow, differentially affect -the two thermistors 10 and 12. For example, i:E the flow of the fluid is horizontally to the right in Figure 1, the temperature experienced at and measured by the thermistor 12 will be higher than the temperature sensed at 10 and this temperature differential is measured by the volt meter 30 as will be readily apparent. Thus, in effect, the distortion of the thermal field established by the heater 14 is mapped by the sensing means 10 and 12, with the amplitude o the voltage reading at the meter 30 being indicative of the degree of deviation or dis-tortion of the thermal field. We have found that thedifferential reading measured at 30 between sensing means diametrically located with respsect to each other on opposite sides of the location of the heater 14 -Erom which the thermal field emanates and wherein this diametrical orientation is aligned with the direction of fluid flow, is substantially linearly related to the flow velocity of the fluid. This is illustrated in Figure 2, the ordinate representing the temperature differential between paired thermistors oriented along the direction ~ 6 --17~
of flow for various calculated rates of 1uid flow through a porous, permeable medium.
Figure 5, appearing on the sheet of drawing containing Figures 1 and 2, illustrates another rela-tionship which obtains at the low groundwater velocities noted in Figure 2, namely, that the peak temperature differential and, hence, voltage differential between thermistors aligned along the airection of ~low as aforesaid occurs approximately three minutes subsequent to initiation of the heat pulse at the heater 14, irrespecti~e of the flow rate within the range depicted.
Figure 3 illustrates a practical embodiment of the present invention and shows a somewhat more detailed electrical circuit arrangement following the principles illustrated in Figure 1. In Figure 3, a suitable source of external voltage is indicated at 32, 34 with the positive side 32 being connected through a manually operated power on/offswitch 36 to the main input line 38. The negative side 3~ o~ the source is connected throuyh a manual pushbutton 38 as an input to the standard 555 type timer indicated generally by the reference 40 so that when the switch 38 is depressed, the timer actuates the constant power circuit for a set period of 30 seconds. In the embodiment of Figure 3, operation of the timer 40 causes the relay coil 42 to be energized correspondingly to actuate the two switches 44 and 46 thereof, the circuit through the solenoid or relay coil 42 being completed through the NPN
;
~'7'~7~
device indicated generally by the reference character 48.
The Device 48 is normally non-conductin.g but when -the timer 555 is energized by depression of the pushbutton 38, the output at pin number 3 thereof, as indicated by the reference character 50,biases the transistor 48 on to allow the relay coil 42 to be energi2ed for the period of time taken before the timer 40 times out. Since the type 555 timer is so well known, only the pin connections thereof are illustrated and the necessary external component connections thereto for providing a thirty second duration energization of the relay coil 42.
When the coil 42 is energized, the switch 44 completes the circuit through the heater 14, which may be provided with a suitable constant power source indicated by the battery 52. The constant power circuit supplies an electrica]. resistance heater 14 which corresponds to the similarly reference heater in Figure 1, although shown for convenience in a separate position in Figure 3, but which is actually disposed centrally wi.th respect to the planar, circular array 54 of thermistor elements 56. After the heater has been energized for the period of time determined by the timer 40, the relay coil 42 is deenergized and the :
switches 44 and 46 return to the full line position shown in Figure 3. In this position, the heater 14 is no longer energized and the switch 46 connects the main power line 38 to the appropriate source voltage input pin of the liquid crystal display device indicated generally by the ~., ~72~7'~
reference character 58. The device 58 illustrated is a DATEL DIGITAL PANE~ METER (1.999V Model DS-3100U2I) with external span adjust capability provided by a lOK variable potentiometer The rotary.switch 64 is employed to measure difference between the analog high and analog low inputs from diametrically opposed pairs of the thermistors 56 of the array 54, such being indicated by reference characters 60 and 62. The array 54 of sensors comprises a circular arrangement thereof about the common center whereat the heater 14 is located as previously mentioned, so that the diametrically opposed pairs of sensors provide, through the rotary switch 64, the respective high and low inputs at 60 and 62 as illustrated. The potentiometer 68 is provided so that its top 66 may be adjusted to provide the proper reference voltage input to the device 58.
Figure 6 illustrates a solid state version of that portion of the electrical system of Fi.gure 3 which eliminates the relay 42, 44, 46 and provide.s a constant power source to replace the battery 52. As shown, a transistor 48 of the type used in Figure 3 is retained and is used in conjunction with the diode 100 to eliminate the need for mechanical switching. ~he operational ampli-fier 102, diode 103, transistors 104 and 106 of types lN1711 and MJ3001 respectively and connected as shown in Darlington array, and the multiplier 108 form a constant power source for the heater 14 when the timing circuit is actuated. The DC-DC converter 110 is provided to supp].y the voltages necessary for the devices :L02 and 108.
~- _ g _ 1~7'~~7~
As noted, the circuit portion shown in Figure 6 is illus-trated merely to show that an all solid state arrangement may be preferable.
Figure 4 illustrates another form of the invention for measuriny groundwater flow. A probe assembly which is indicated generally by the reference character 70 comprises a porous mass of particulate material indicated by the reference character 72, having a heat conductivity of at least 10 times that of water and, imbedded therein, are a heater element 74 and a surrounding array of sensors 76, 78, 80, 82, 84 and 86. The sensors 76, 80, 82 and 86 lie in a common plane and are disposed in diametrically opposed pairs whereas the sensors 76, 78, 82 and 84 lie in a second plane orthogonal ~to the first-mentioned plane and, again, arranged in diametrically opposed pairs and, lastly, the sensors 78, 80, 84 and 86 lie in a third, orthogonal plane whereby the heater element 74 lies at the center of the spherical surface upon which the various sensors lie. IE, now, the line through the sensors 76 and 82 is oriented in the North direction as indicated, and the outputs of the various sensors are connected as inputs to an X, Y, Z
comparator and computer 88, the precise direction o~
groundwater flow through the permeable structure 72 may be recorded by the mechanism 90 in accordance with well-known X, Y, Z resolution techniques. At the same time, the flow rate is computed by determination of the temper-ature differential between diametrically opposed points, in the horizontal plane containing the sensors 76, 80, 82 and 86, which are aligned with the flow dlrection 1~7Z~7~
The pu~pose o~ the porous structure 72 is not only accurately to position the sensors and heater and to provide the proper heat conductivity -to produce the afore-said thermal field but also to provide a probe which is useful in a variety of soils. For example, although the heaters and sensors may be arrayed directly in rather small grained soils to obtain accurate measurements of direction and flow velocity, large grain size soils may give inaccurate readings because of distortions to the thermal field caused by the soil particles themselves.
Thus, the porous structure 72 consists of an agglomeration of similarly sized small particles through which the groundwater flows so as uniformly to affect the various sensors with respect to the thermal field generated by the heater 74~
The heater and sensor array can be inserted directly into the water saturated zone of fine gravel to fine sand soil to measure the rate and direction of ground-water flow or may be enclosed or encased in an end cap o~ porous spherical material of suitable permeability.
Water moving through the irregular soil pores courses through the permeahle substrate into which the sensing elements and heater are situated. The flow is laminar and continuous under normal groundwater flow conditions (V = 30 ft. per day or less) flow through the porous end cap continues to be laminar without the formation of any boundary layers between probe and the water saturated natural soil into which the probe is immersed. No stagnation points exist, as in the case of fluid flow around nonporous probes To sense the direction and rate ~7~87~
of -flow, the probe is first oriented towards magne-tic North, Each opposing pair of sensors is nulled to zero or a stable difference recorded, As portraye~l in Figure 1, a heat pulse is released into the porous substrate and moves symmetric-ally outwards in all directions, The natural laminar flow of groundwater influences the thermal field in the porous solid, retarding the outward flow of heat at a maximum in the direction in which laminar flow directly opposes heat flow and augmenting the outward flow at a maximum in the direction of the laminar flow, Sensors lying perpendicular to the axis of flow would show no variation due to laminar flow, since the distortion of the thermal field moving through the solid matrix would remain equivalent for each.
The probe can be used in naturally porous soils from fine gravel to fine silty sand. As the particle size approaches that of medium gravel, the pathways of inter-stitial -flow become too irreyular to measure direction accurately. Similarly, variations in heat conductance through larye particles (intra-particle conductance) dominate heat transfer between particles (inter-particle conductance), which leads to high variability in estimating flow rate, ~hus, for measuring flow rates in gravel, it is essential that the array be embedded in the porous mass 72 as shown in Figure 4, the mass 72 being composed of uni-form spherical particles within the range of 1-.1 mm diameter as long as the flow velocity through the gravel is not so high as to be excessively impeded by the permeability of the porous mass, The vec-tor field indica-ted by the amplitude of opposing pairs of heat sensors can provide additional 37'~
in~ormation on the characteristics of yroundwater flow apart from direction and rate of fLow. For the first example, uniform horizontal flow occurs, all vectors will correspond to the cosine of the vector solution ~or primary direction of flow). However, if the column of water is unstable vertically, the vectors will deviate from the cosine of the direction of principal flow.
Described mathematically by the function:
y - acos~
where: y = the rate of flow in a direction (x) a = the rate of 10w i~ the principle direction of flow x = the angle of deviation from the direction of main flow.
For a second example, if the water mass has an oscillating nature, moving back.and forth with a period less than that for a reading, the heat flux field will describe the main components of that motion, If the water mass has an oscillating nature with a period substantially greater than that of the time required for measurement, such as groundwater in coastal areas sub-jected to tidal action, successive recordings at appropriate intervals can be employed to describe the harmonics of the oscillatory motion Lastly, if an array of three probe units are inserted into shallow surface groundwater in a triangular arrangement, the units can be used to detect the position and approximate volume of displacement of a transient dis-charge of water or liquid occurring between or nearby the array Continual recordi.ng of the independent probes can 37~
establish the background flow conditions of rate and direc-tion. Any sudden addition of volume to groundwater surface creates an outwards rush of shallow groundwater displacing the recorded principal direction of flow at the independent units in a direction emanating from that of the source of the displacement and proportional to the volume added.
Detection is quite rapid, as the introduced mass of liquid need not reach the sensors, only the head differential due to the propagated displacement.
In addition to detecting a discharge, a triangular array can also be used surrounding a wi-thdrawal well to a sure movement within the boundary property. With either treatment of the withdrawn water or evaporation of the pumped water, the monitoring system can be used to isolate the local groundwater movement to form a flow cell so that no groundwater flow will leave the property.
~ lthouyh this invention is directed principally to the measurement of direction and/or rate of groundwater flow in order to determi.ne the environmental effect, for example, of septic leachate upon natural water systems, the basic principles of this invention are applicable to a wide range of problems in which the velocity and/or direction of fluid flow is in question.
At present, many systems and techniques have been developed to provide information about the direction and/or rate of a fluid flow, including systems which rely on steady state heating a tube through which a liquid flows and measuring temperatures of the moving li~uid at upstream and downstream locations relative to the heat source, to obtain a hyperbolic measurement of flow rate. However, none has to my knowledge been developed which involves measurement of the distortion of a thermal field established by locally heating a permeable mass through which the f].uid flows, to obtain a linear measurement of fluid flow rate.
rrhis invent.ion relates to the discovery that the distortion of a thermal field established in a porous medium through which a very slowly flowing groundwater system moves, can be used to provide a linear measurement of the rate of such groundwater flow. ~ore specifically, it was found that if temperature measurements are made at different regions of the distorted field, so as in effect to "map" it, not only can the flow azimuth be determined, but also the rate of flow can be determined.
In a basic arrangement, the thermal field is established by transferring a predetermined quantity of heat energy to a highly localized region of a porous heat ~72~7'~
conductive medium through which the groundwater flows.
The localized region is at -the center o~ a surrounding array of ternperature sensors. By not.ing the temperature change differential between diametrically opposed pairs of sensors, the pair indicating the greatest such differ-ential provides information concerning the direction of flow whereas the amplitude o~ the differential provides a linear indication of the rate of flow.
In such system, the heat source was "pulsed"
whereafter the maximum temperature differentials between the pairs of the sensors were recorded. It was discovered that over a wide ran~e of groundwater flow velocities, the temperature differentials peaked after the same elapsed time subsequent to cessation of the heat "pulse", and that the variation in maximum temperature differential in the direction of flow, was essentially linearly related to groundwater flow rate of velocity.
Figure 1 is a schematic diagram illustrating certain basic features of the invention, Figure 2 is a graph illustrating the li~earity between maximum temperature differential and fluid flow rate, Figure 3 is a schematic illustrating one embodiment of the invention, Figure 4 is a schematic view illustrating one embodiment of a proble assembly and associated measuring circuitry, Figure 5 is a graph illustrating certain properties of the invention, and 2~
Figure 6 is a circuit diagram showing a modified form of the control assembly Referring more particularly to Figure 1, certair.
principles of the present invention will be apparent therefrom. As illustrated, a pair of temperature sensing means 10 and 12 and which in the specific construction illustrated take the form of termistors, are arrayed on opposite sides of a heating element indicated generally by the reference character 14. It will be understood that the sensing means 10 and 12 as well as the heater 14 are to be disposed within a porous heat conductive medium M through which the fluid whose flow character-istics are being measured, flows. In the groundwater system, the porous medium can be the soil itself, in which case the naked heater and sensor may be inserted thereinto. However, the sensing means and the heater are preferably embedded in a porous or permeable mass to provide a probe element to assure uniform and accurate heat conductivity. When such an arrangement is used, the porous mass should be formed of substantially uni-formly sized spherical particles having heat conductivity substantially greater than that of the fluid whose flow is being measured, the particle size being not greater than about 1.0 mm in diameter and sufficiently large as will not impede, distort or adversely affect the normal groundwater flow.
~'7ZB7~
In any even, with the arrangement as shown, a timer indicated generally by the reference character 16 is actuated by suitable means not illustrated to energize the heater 14 from the power source 18 for a predeter-mined period of time In this way, a predetermined quantity of thermal energy is introduced, the ammeter 20 being illustrated in the line connection to the heater 14 to illustrate this fact, i.e~, that the arrangement is such as to provide a control power input to the heater 14 such that the heater dissipates a predetermined quantity of heat conductive medium during a predetermined period of time controlled by the timer 16.
In this fashion, the heater 14 is "pulsed" to heat the porous mass M and establish a thermal field within the flow path of the fluid whose flow character-istics are being measured. In the absence of fluid flow or movement, the field is centered about the location of the heater 14 and is symmetrical or of predetermined shape with respect thereto.
The two thermistors 10 and 12 are connected to a suitable source 22 and the two branches of the circuitry to the individual sensors 10 and 12 include, in addition to the variable resistance displayed by the sensors, the resistors 2~ and 26 respectively and a common variable resistance element 28 suitably grounded as shown to ~L~72~7~
connect the opposite side of the supply 22. The two resistors 24 and 26 are o~ equal value and the resistor 28 is variable to establish a calibrated set point or zero at the volt meter 30 at some predetermined temper-ature of the two thermistors 10 and 12 The aforementioned thermal field, in the presence of fluid movement or flow, will be distorted and the deviation represented thereby will, dependent upon the direction of flow, differentially affect -the two thermistors 10 and 12. For example, i:E the flow of the fluid is horizontally to the right in Figure 1, the temperature experienced at and measured by the thermistor 12 will be higher than the temperature sensed at 10 and this temperature differential is measured by the volt meter 30 as will be readily apparent. Thus, in effect, the distortion of the thermal field established by the heater 14 is mapped by the sensing means 10 and 12, with the amplitude o the voltage reading at the meter 30 being indicative of the degree of deviation or dis-tortion of the thermal field. We have found that thedifferential reading measured at 30 between sensing means diametrically located with respsect to each other on opposite sides of the location of the heater 14 -Erom which the thermal field emanates and wherein this diametrical orientation is aligned with the direction of fluid flow, is substantially linearly related to the flow velocity of the fluid. This is illustrated in Figure 2, the ordinate representing the temperature differential between paired thermistors oriented along the direction ~ 6 --17~
of flow for various calculated rates of 1uid flow through a porous, permeable medium.
Figure 5, appearing on the sheet of drawing containing Figures 1 and 2, illustrates another rela-tionship which obtains at the low groundwater velocities noted in Figure 2, namely, that the peak temperature differential and, hence, voltage differential between thermistors aligned along the airection of ~low as aforesaid occurs approximately three minutes subsequent to initiation of the heat pulse at the heater 14, irrespecti~e of the flow rate within the range depicted.
Figure 3 illustrates a practical embodiment of the present invention and shows a somewhat more detailed electrical circuit arrangement following the principles illustrated in Figure 1. In Figure 3, a suitable source of external voltage is indicated at 32, 34 with the positive side 32 being connected through a manually operated power on/offswitch 36 to the main input line 38. The negative side 3~ o~ the source is connected throuyh a manual pushbutton 38 as an input to the standard 555 type timer indicated generally by the reference 40 so that when the switch 38 is depressed, the timer actuates the constant power circuit for a set period of 30 seconds. In the embodiment of Figure 3, operation of the timer 40 causes the relay coil 42 to be energized correspondingly to actuate the two switches 44 and 46 thereof, the circuit through the solenoid or relay coil 42 being completed through the NPN
;
~'7'~7~
device indicated generally by the reference character 48.
The Device 48 is normally non-conductin.g but when -the timer 555 is energized by depression of the pushbutton 38, the output at pin number 3 thereof, as indicated by the reference character 50,biases the transistor 48 on to allow the relay coil 42 to be energi2ed for the period of time taken before the timer 40 times out. Since the type 555 timer is so well known, only the pin connections thereof are illustrated and the necessary external component connections thereto for providing a thirty second duration energization of the relay coil 42.
When the coil 42 is energized, the switch 44 completes the circuit through the heater 14, which may be provided with a suitable constant power source indicated by the battery 52. The constant power circuit supplies an electrica]. resistance heater 14 which corresponds to the similarly reference heater in Figure 1, although shown for convenience in a separate position in Figure 3, but which is actually disposed centrally wi.th respect to the planar, circular array 54 of thermistor elements 56. After the heater has been energized for the period of time determined by the timer 40, the relay coil 42 is deenergized and the :
switches 44 and 46 return to the full line position shown in Figure 3. In this position, the heater 14 is no longer energized and the switch 46 connects the main power line 38 to the appropriate source voltage input pin of the liquid crystal display device indicated generally by the ~., ~72~7'~
reference character 58. The device 58 illustrated is a DATEL DIGITAL PANE~ METER (1.999V Model DS-3100U2I) with external span adjust capability provided by a lOK variable potentiometer The rotary.switch 64 is employed to measure difference between the analog high and analog low inputs from diametrically opposed pairs of the thermistors 56 of the array 54, such being indicated by reference characters 60 and 62. The array 54 of sensors comprises a circular arrangement thereof about the common center whereat the heater 14 is located as previously mentioned, so that the diametrically opposed pairs of sensors provide, through the rotary switch 64, the respective high and low inputs at 60 and 62 as illustrated. The potentiometer 68 is provided so that its top 66 may be adjusted to provide the proper reference voltage input to the device 58.
Figure 6 illustrates a solid state version of that portion of the electrical system of Fi.gure 3 which eliminates the relay 42, 44, 46 and provide.s a constant power source to replace the battery 52. As shown, a transistor 48 of the type used in Figure 3 is retained and is used in conjunction with the diode 100 to eliminate the need for mechanical switching. ~he operational ampli-fier 102, diode 103, transistors 104 and 106 of types lN1711 and MJ3001 respectively and connected as shown in Darlington array, and the multiplier 108 form a constant power source for the heater 14 when the timing circuit is actuated. The DC-DC converter 110 is provided to supp].y the voltages necessary for the devices :L02 and 108.
~- _ g _ 1~7'~~7~
As noted, the circuit portion shown in Figure 6 is illus-trated merely to show that an all solid state arrangement may be preferable.
Figure 4 illustrates another form of the invention for measuriny groundwater flow. A probe assembly which is indicated generally by the reference character 70 comprises a porous mass of particulate material indicated by the reference character 72, having a heat conductivity of at least 10 times that of water and, imbedded therein, are a heater element 74 and a surrounding array of sensors 76, 78, 80, 82, 84 and 86. The sensors 76, 80, 82 and 86 lie in a common plane and are disposed in diametrically opposed pairs whereas the sensors 76, 78, 82 and 84 lie in a second plane orthogonal ~to the first-mentioned plane and, again, arranged in diametrically opposed pairs and, lastly, the sensors 78, 80, 84 and 86 lie in a third, orthogonal plane whereby the heater element 74 lies at the center of the spherical surface upon which the various sensors lie. IE, now, the line through the sensors 76 and 82 is oriented in the North direction as indicated, and the outputs of the various sensors are connected as inputs to an X, Y, Z
comparator and computer 88, the precise direction o~
groundwater flow through the permeable structure 72 may be recorded by the mechanism 90 in accordance with well-known X, Y, Z resolution techniques. At the same time, the flow rate is computed by determination of the temper-ature differential between diametrically opposed points, in the horizontal plane containing the sensors 76, 80, 82 and 86, which are aligned with the flow dlrection 1~7Z~7~
The pu~pose o~ the porous structure 72 is not only accurately to position the sensors and heater and to provide the proper heat conductivity -to produce the afore-said thermal field but also to provide a probe which is useful in a variety of soils. For example, although the heaters and sensors may be arrayed directly in rather small grained soils to obtain accurate measurements of direction and flow velocity, large grain size soils may give inaccurate readings because of distortions to the thermal field caused by the soil particles themselves.
Thus, the porous structure 72 consists of an agglomeration of similarly sized small particles through which the groundwater flows so as uniformly to affect the various sensors with respect to the thermal field generated by the heater 74~
The heater and sensor array can be inserted directly into the water saturated zone of fine gravel to fine sand soil to measure the rate and direction of ground-water flow or may be enclosed or encased in an end cap o~ porous spherical material of suitable permeability.
Water moving through the irregular soil pores courses through the permeahle substrate into which the sensing elements and heater are situated. The flow is laminar and continuous under normal groundwater flow conditions (V = 30 ft. per day or less) flow through the porous end cap continues to be laminar without the formation of any boundary layers between probe and the water saturated natural soil into which the probe is immersed. No stagnation points exist, as in the case of fluid flow around nonporous probes To sense the direction and rate ~7~87~
of -flow, the probe is first oriented towards magne-tic North, Each opposing pair of sensors is nulled to zero or a stable difference recorded, As portraye~l in Figure 1, a heat pulse is released into the porous substrate and moves symmetric-ally outwards in all directions, The natural laminar flow of groundwater influences the thermal field in the porous solid, retarding the outward flow of heat at a maximum in the direction in which laminar flow directly opposes heat flow and augmenting the outward flow at a maximum in the direction of the laminar flow, Sensors lying perpendicular to the axis of flow would show no variation due to laminar flow, since the distortion of the thermal field moving through the solid matrix would remain equivalent for each.
The probe can be used in naturally porous soils from fine gravel to fine silty sand. As the particle size approaches that of medium gravel, the pathways of inter-stitial -flow become too irreyular to measure direction accurately. Similarly, variations in heat conductance through larye particles (intra-particle conductance) dominate heat transfer between particles (inter-particle conductance), which leads to high variability in estimating flow rate, ~hus, for measuring flow rates in gravel, it is essential that the array be embedded in the porous mass 72 as shown in Figure 4, the mass 72 being composed of uni-form spherical particles within the range of 1-.1 mm diameter as long as the flow velocity through the gravel is not so high as to be excessively impeded by the permeability of the porous mass, The vec-tor field indica-ted by the amplitude of opposing pairs of heat sensors can provide additional 37'~
in~ormation on the characteristics of yroundwater flow apart from direction and rate of fLow. For the first example, uniform horizontal flow occurs, all vectors will correspond to the cosine of the vector solution ~or primary direction of flow). However, if the column of water is unstable vertically, the vectors will deviate from the cosine of the direction of principal flow.
Described mathematically by the function:
y - acos~
where: y = the rate of flow in a direction (x) a = the rate of 10w i~ the principle direction of flow x = the angle of deviation from the direction of main flow.
For a second example, if the water mass has an oscillating nature, moving back.and forth with a period less than that for a reading, the heat flux field will describe the main components of that motion, If the water mass has an oscillating nature with a period substantially greater than that of the time required for measurement, such as groundwater in coastal areas sub-jected to tidal action, successive recordings at appropriate intervals can be employed to describe the harmonics of the oscillatory motion Lastly, if an array of three probe units are inserted into shallow surface groundwater in a triangular arrangement, the units can be used to detect the position and approximate volume of displacement of a transient dis-charge of water or liquid occurring between or nearby the array Continual recordi.ng of the independent probes can 37~
establish the background flow conditions of rate and direc-tion. Any sudden addition of volume to groundwater surface creates an outwards rush of shallow groundwater displacing the recorded principal direction of flow at the independent units in a direction emanating from that of the source of the displacement and proportional to the volume added.
Detection is quite rapid, as the introduced mass of liquid need not reach the sensors, only the head differential due to the propagated displacement.
In addition to detecting a discharge, a triangular array can also be used surrounding a wi-thdrawal well to a sure movement within the boundary property. With either treatment of the withdrawn water or evaporation of the pumped water, the monitoring system can be used to isolate the local groundwater movement to form a flow cell so that no groundwater flow will leave the property.
Claims (21)
1. The method of measuring a flow characteristic of a fluid, which comprises the steps of:
(a) providing a heat conductive porous medium;
(b) heating a localized region of said heat conductive porous medium through which fluid is flowing, the heat conductivity of the porous medium being substantially greater than the heat conductivity of the fluid; and (c) measuring the temperature of the medium at at least two regions spaced from said localized region and determining a flow characteristic of the fluid therefrom.
(a) providing a heat conductive porous medium;
(b) heating a localized region of said heat conductive porous medium through which fluid is flowing, the heat conductivity of the porous medium being substantially greater than the heat conductivity of the fluid; and (c) measuring the temperature of the medium at at least two regions spaced from said localized region and determining a flow characteristic of the fluid therefrom.
2. The method of measuring a flow characteristic of a fluid, which comprises the steps of:
(a) heating a localized region of a heat conductive medium through which fluid is flowing, the heat conductivity of the medium being substantially greater than the heat conductivity of the fluid;
(b) measuring the temperature of the medium at at least two regions spaced from said localized region and determining a flow characteristic of the fluid therefrom;
and (c) performing the heating of step (a) by heating the medium for a short period of time at said localized region and performing step (b) subsequent to such heating.
(a) heating a localized region of a heat conductive medium through which fluid is flowing, the heat conductivity of the medium being substantially greater than the heat conductivity of the fluid;
(b) measuring the temperature of the medium at at least two regions spaced from said localized region and determining a flow characteristic of the fluid therefrom;
and (c) performing the heating of step (a) by heating the medium for a short period of time at said localized region and performing step (b) subsequent to such heating.
3. The method as defined in claim 1 wherein the measurement step is made by temperature sensing means displaced from said location
4. The method as defined in claim 2 wherein the measurement step is made by temperature sensing means displaced from said location.
5. The method as defined in claim 3 wherein said temperature sensing means are arranged in an array surround-ing said location.
6. The method as defined in claim 4 wherein said temperature sensing means are arranged in an array surround-ing said location.
7. The method as defined in either claim 1 or 2 wherein the measurement step is a peak temperature measuring.
8. The method of measuring flow characteristics of a fluid, which comprises the steps of:
(a) establishing a thermal field represented by temperature peaks in a porous medium disposed within the fluid under test, the heat conductivity of the medium being at least 10 times greater than the heat conductivity of the fluid;
(b) measuring temperature peaks within different regions of the thermal field; and (c) determining a flow characteristic of the fluid from the measurements of step (b).
(a) establishing a thermal field represented by temperature peaks in a porous medium disposed within the fluid under test, the heat conductivity of the medium being at least 10 times greater than the heat conductivity of the fluid;
(b) measuring temperature peaks within different regions of the thermal field; and (c) determining a flow characteristic of the fluid from the measurements of step (b).
9. The method as defined in claim 8 wherein the flow characteristic determined in step (c) is flow direction.
10. The method as defined in claim 8 wherein the flow characteristic determined in step (c) is flow velocity.
11. The method as defined in claim 8 wherein both flow direction and flow velocity are determined in step (c).
12. The method of measuring the direction of flow of a fluid, which comprises the steps of:
(a) positioning a porous medium in the flowing fluid, said medium having an array of temperature sensors therein and having heat conductivity much greater than that of the fluid;
(b) heating the medium for a short period of time at a localized position spaced from said sensors thereby creating temperature peaks;
(c) measuring the temperature peaks at said sensors due to the heat applied in step (a) subsequent to cessation of the heating of step (b); and (d) determining the direction of fluid flow from the measurements of step (c).
(a) positioning a porous medium in the flowing fluid, said medium having an array of temperature sensors therein and having heat conductivity much greater than that of the fluid;
(b) heating the medium for a short period of time at a localized position spaced from said sensors thereby creating temperature peaks;
(c) measuring the temperature peaks at said sensors due to the heat applied in step (a) subsequent to cessation of the heating of step (b); and (d) determining the direction of fluid flow from the measurements of step (c).
13. The method of measuring the direction and rate of flow of a fluid, which comprises the steps of:
(a) positioning a porous medium in the flowing fluid, said medium having an array of temperature sensors therein and having heat conductivity much greater than that of the fluid;
(b) heating the medium for a short period of time at a localized position spaced from said sensors thereby creating temperature peaks;
(c) measuring the temperature peaks at said sensors due to the heat applied in step (b) subsequent to cessation of the heating of step (b); and (d) determining the direction and rate of flow of the fluid from the measurements of step (c).
(a) positioning a porous medium in the flowing fluid, said medium having an array of temperature sensors therein and having heat conductivity much greater than that of the fluid;
(b) heating the medium for a short period of time at a localized position spaced from said sensors thereby creating temperature peaks;
(c) measuring the temperature peaks at said sensors due to the heat applied in step (b) subsequent to cessation of the heating of step (b); and (d) determining the direction and rate of flow of the fluid from the measurements of step (c).
14. The method of measuring the rate of flow of a fluid, which comprises the steps of:
(a) positioning a porous medium in the flowing fluid, said medium having a pair of temperature sensors therein which are spaced apart in the direction of flow of the fluid whose flow rate is to be measured and having heat conductivity much greater than that of the fluid;
(b) heating the medium for a short period of time at a localized position spaced between said temperature sensors;
represented by differential temperature peaks;
(c) measuring the peak temperature differential between said sensors due to the heat applied in step (b) subsequent to cessation of the heating of step (b); and (d) determining the rate of fluid flow from the measurement of step (c).
(a) positioning a porous medium in the flowing fluid, said medium having a pair of temperature sensors therein which are spaced apart in the direction of flow of the fluid whose flow rate is to be measured and having heat conductivity much greater than that of the fluid;
(b) heating the medium for a short period of time at a localized position spaced between said temperature sensors;
represented by differential temperature peaks;
(c) measuring the peak temperature differential between said sensors due to the heat applied in step (b) subsequent to cessation of the heating of step (b); and (d) determining the rate of fluid flow from the measurement of step (c).
15. The method of measuring the direction and rate of flow of a fluid, which comprises the steps of:
(a) positioning a porous medium in the flowing fluid, said medium having an array of temperature sensors therein and having heat conductivity much greater than that of the fluid;
(b) heating the medium for a short period of time at a localized position spaced from said sensors thereby creating temperature peaks;
(c) measuring the temperature peaks at said sensors due to the heat applied in step (b) subsequent to cessation of the heating of step (b);
(d) determining the direction and rate of flow of the fluid from the measurements of step (c); and (e) said first means comprises a heater and circuitry for energizing said heater for a predetermined time.
(a) positioning a porous medium in the flowing fluid, said medium having an array of temperature sensors therein and having heat conductivity much greater than that of the fluid;
(b) heating the medium for a short period of time at a localized position spaced from said sensors thereby creating temperature peaks;
(c) measuring the temperature peaks at said sensors due to the heat applied in step (b) subsequent to cessation of the heating of step (b);
(d) determining the direction and rate of flow of the fluid from the measurements of step (c); and (e) said first means comprises a heater and circuitry for energizing said heater for a predetermined time.
16. The method of measuring the direction and rate of flow of a fluid, which comprises the steps of:
(a) positioning a porous medium in the flowing fluid, said medium having an array of temperature sensors therein and having heat conductivity much greater than that of the fluid;
(b) heating the medium for a short period of time at a localized position spaced from said sensors thereby creating temperature peaks;
(c) measuring the temperature peaks at said sensors due to the heat applied in step (b) subsequent to cessation of the heating of step (b);
(d) determining the direction and rate of flow of the fluid from the measurements of step (c); and (e) said second means comprises an array of temperature sensors disposed within said medium.
(a) positioning a porous medium in the flowing fluid, said medium having an array of temperature sensors therein and having heat conductivity much greater than that of the fluid;
(b) heating the medium for a short period of time at a localized position spaced from said sensors thereby creating temperature peaks;
(c) measuring the temperature peaks at said sensors due to the heat applied in step (b) subsequent to cessation of the heating of step (b);
(d) determining the direction and rate of flow of the fluid from the measurements of step (c); and (e) said second means comprises an array of temperature sensors disposed within said medium.
17. The method of measuring the direction and rate of flow of a fluid, which comprises the steps of:
(a) positioning a porous medium in the flowing fluid, said medium having an array of temperature sensors therein and having heat conductivity much greater than that of the fluid;
(b) heating the medium for a short period of time at a localized position spaced from said sensors thereby creating temperature peaks;
(c) measuring the temperature peaks at said sensors due to the heat applied in step (b) subsequent to cessation of the heating of step (b);
(d) determining the direction and rate of flow of the fluid from the measurements of step (c); and (e) said first means comprises a heater and said second means comprises a plurality of temperature sensors arrayed symmetrically with respect to said heater.
(a) positioning a porous medium in the flowing fluid, said medium having an array of temperature sensors therein and having heat conductivity much greater than that of the fluid;
(b) heating the medium for a short period of time at a localized position spaced from said sensors thereby creating temperature peaks;
(c) measuring the temperature peaks at said sensors due to the heat applied in step (b) subsequent to cessation of the heating of step (b);
(d) determining the direction and rate of flow of the fluid from the measurements of step (c); and (e) said first means comprises a heater and said second means comprises a plurality of temperature sensors arrayed symmetrically with respect to said heater.
18. The method of measuring the direction and rate of flow of a fluid, which comprises the steps of:
(a) positioning a porous medium in the flowing fluid, said medium having an array of temperature sensors therein and having heat conductivity much greater than that of the fluid;
(b) heating the medium for a short period of time at a localized position spaced from said sensors thereby creating temperature peaks;
(c) measuring the temperature peaks at said sensors due to the heat applied in step (b) subsequent to cessation of the heating of step (b);
(d) determining the direction and rate of flow of the fluid from the measurements of step (c); and (e) said second means also includes means for determining peak temperature differentials between certain pairs of said sensors.
(a) positioning a porous medium in the flowing fluid, said medium having an array of temperature sensors therein and having heat conductivity much greater than that of the fluid;
(b) heating the medium for a short period of time at a localized position spaced from said sensors thereby creating temperature peaks;
(c) measuring the temperature peaks at said sensors due to the heat applied in step (b) subsequent to cessation of the heating of step (b);
(d) determining the direction and rate of flow of the fluid from the measurements of step (c); and (e) said second means also includes means for determining peak temperature differentials between certain pairs of said sensors.
19. Method according to claim 17 wherein said second means also includes means for determining peak temperature differentials between certain pairs of said sensors.
20. The method of obtaining a linear measurement of capillary groundwater flow which comprises the steps of:
(a) providing a porous mass composed of uniform spherical particles having a diameter within the range of 0.1-1.0 mm and a heat conductivity of at least 10 times that of water and having an array of heat sensors embedded therein and a heating source centrally disposed among said sensors;
(b) embedding the porous mass within the ground so as to be exposed to groundwater flow;
(c) energizing said source for a predetermined time;
(d) measuring the peak differentials in temperature exhibited between diametrically opposed sensors of said arrays; and (e) determining groundwater flow as a linear function of the maximum peak differential measured in step (d).
(a) providing a porous mass composed of uniform spherical particles having a diameter within the range of 0.1-1.0 mm and a heat conductivity of at least 10 times that of water and having an array of heat sensors embedded therein and a heating source centrally disposed among said sensors;
(b) embedding the porous mass within the ground so as to be exposed to groundwater flow;
(c) energizing said source for a predetermined time;
(d) measuring the peak differentials in temperature exhibited between diametrically opposed sensors of said arrays; and (e) determining groundwater flow as a linear function of the maximum peak differential measured in step (d).
21. The method as defined in claim 20 including the step of orienting the array, in step (b), such that the azimuths of diametrically opposed pairs of sensors is known and including the additional step of determining groundwater flow direction in step (e).
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEP3024417.8 | 1980-06-28 | ||
| DE19803024417 DE3024417A1 (en) | 1980-06-28 | 1980-06-28 | METHOD AND DEVICE FOR MEASURING A FLOW CHARACTERISTIC |
| US06/276,787 US4391137A (en) | 1980-06-28 | 1981-06-24 | Groundwater flow meter |
| US276,787 | 1981-06-24 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1172872A true CA1172872A (en) | 1984-08-21 |
Family
ID=25786276
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000380663A Expired CA1172872A (en) | 1980-06-28 | 1981-06-26 | Groundwater flow meter |
Country Status (6)
| Country | Link |
|---|---|
| AT (1) | AT386685B (en) |
| CA (1) | CA1172872A (en) |
| GB (1) | GB2079470B (en) |
| NL (1) | NL8103134A (en) |
| NO (1) | NO155217C (en) |
| SE (1) | SE441962B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2552208B1 (en) * | 1983-09-16 | 1988-01-22 | Gaz De France | METHOD AND DEVICE FOR INTERRUPTING THE OPERATION OF AN APPARATUS USING A GASEOUS FLUID |
| US5551287A (en) * | 1995-02-02 | 1996-09-03 | Mobil Oil Corporation | Method of monitoring fluids entering a wellbore |
| DE102006012229B3 (en) | 2006-03-16 | 2007-06-14 | Siemens Ag | Cooling fluid`s flow measuring device for electric machine, has measuring unit with optical fiber cables, and evaluating unit evaluating temperature influence of shaft depending on individual heat flow directed from heating unit to cables |
-
1981
- 1981-06-26 AT AT0286781A patent/AT386685B/en not_active IP Right Cessation
- 1981-06-26 NO NO812198A patent/NO155217C/en unknown
- 1981-06-26 GB GB8119772A patent/GB2079470B/en not_active Expired
- 1981-06-26 CA CA000380663A patent/CA1172872A/en not_active Expired
- 1981-06-29 NL NL8103134A patent/NL8103134A/en not_active Application Discontinuation
- 1981-06-29 SE SE8104053A patent/SE441962B/en not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| GB2079470A (en) | 1982-01-20 |
| SE441962B (en) | 1985-11-18 |
| NL8103134A (en) | 1982-01-18 |
| AT386685B (en) | 1988-09-26 |
| GB2079470B (en) | 1984-10-31 |
| NO155217B (en) | 1986-11-17 |
| NO155217C (en) | 1987-02-25 |
| SE8104053L (en) | 1981-12-29 |
| NO812198L (en) | 1981-12-29 |
| ATA286781A (en) | 1988-02-15 |
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