APPARATUS AND METHOD FOR CONTROLLING SAND MOISTURE

Abstract: Sand from a hopper (12) is fed onto a conveyor belt (22) in a layer 15 of uniform thickness. The temperature of the sand is measured by a plurality of thermocouples (42) spaced across the width of the layer. The resistivity is measured by measuring the resistance between two parallel conductive plates (40) transversely spaced across the layer. A sensor (44,46) measures the speed of the conveyor and a process controller (300) responds to the measured values and a manually entered desired moisture content signal to control a valve (46) regulating the flow of water into a water mixing device (16), where water is mixed into the sand coming off the conveyor.

Description: This invention relates to apparatus and a method for automatically controlling the moisture content of foundry sand. In foundry operations, foundry sand is mixed with water and used for molds and cores which are in turn used in casting operations. Moisture control is known to be an important factor in obtaining durable molds and cores. It is known to measure the moisture content of foundry sand prior to mixing the sand in a mixer in order to calculate the volume of water that should be added to obtain the correct moisture content. One apparatus is known from US-A 4 569 025 which teaches the automatic measurement of sand moisture content along with other foundry sand parameters, including sand temperatures. The measurement of moisture content can take place on a capacitive basis in the mixer or as the sand is transported to the mixer. A system is also known wherein the moisture content of sand is calculated by measuring the loss of microwave energy through the sand and the temperature of the sand. In this apparatus, a layer of sand is conveyed from a hopper to a mixer along a belt. Microwave energy and infrared temperature measurements are taken as the sand is moved along the belt. Based on these readings and assuming a constant belt speed, a volumetric addition of water is automatically calculated, using an analog circuit, and added to the sand after it enters the hopper. Although the infrared temperature sensors and microwave measurements give precise information on said temperature and moisture content, these methods suffer from restricted sampling area and therefore often lead to wide deviations between the actual and desired sand moisture content. In addition, the volumetric rate of sand transport often varies from its predicted rate therefore leading to additional variations between the actual moisture content of sand leaving the mixer and the desired moisture content of the sand. An apparatus according to the introductory part of claim 1 is known from DE-A 2 627 904 which describes various arrangements in which a volume of sand is compacted before its resistance is measured, including an arrangement of parallel plate electrodes formed as stamps which are moved together to compact sand therebetween. This arrangement does not permit continuous measurements in a constantly moving layer of sand. The object of the present invention is to provide an improved apparatus for automatically measuring the moisture content of the sand with good accuracy notwithstanding the continuous transport thereof on the conveyor. The apparatus according to the invention is characterised in the manner set forth in claim 1. The preferred embodiment uses a conveyor for transporting a substantially uniform layer of sand. With the conveyor there is provided a means for measuring the average temperature of the sand layer across its width and generating a representative temperature signal. Along with the temperature measurement means, a series of electrically conductive members extend into and are spaced transversely across a portion of the sand layer to measure the electrical resistance across the sand layer between the members. Means are also provided for measuring the velocity of the sand layer that moves past the temperature measurement means and the conductive members. The temperature signal and signals representing the electrical resistance and velocity of the sand layer are received by a signal processing unit into which a predetermined moisture content value is entered and which calculates a water addition value that is necessary for the sand to have the predetermined moisture content. The water addition value is used to control a means for adding water to the sand that is located downstream of the temperature measuring means and the resistance members. In a preferred form, this invention uses thermocouples as the sensors for measuring sand temperature and a series of plates spaced transversely to the directional movement of the sand layer to measure electrical resistance across the sand that passes between the plates. Accuracy of the temperature measurement across the sand layer is improved by using a series of thermocouples located at different depths within the sand layer. It has been found that the temperature on the surface of the sand layer is often much lower than the temperature of sand in the middle or bottom of the sand layer. Therefore, taking the temperature reading at several depths in the sand layer gives a more representative value of the average sand temperature. It has also been found that the moisture content of the sand can vary over the layer. Therefore, measurement of incipient sand moisture content is improved by the use of plates for measuring the electrical resistance since the plates may be spaced apart and inserted into the sand layer to measure a relatively large volume of sand and thereby obtain a more accurate value for average resistance which in turn allows calculation of a more reliable value for the overall sand moisture content. In this regard, it has been found that two plates spaced apart transversely with respect to the direction of sand flow and placed with their longitudinal dimension parallel to the direction of sand flow, which are inserted into sand layer by an amount sufficient to measure at least ten percent of the volume of transported sand will provide a satisfactory resistance reading for calculating and controlling the sand moisture content. As stated earlier, transportation of the sand using a belt conveyor has been found to introduce errors in the measurement of the passing sand volume. This error is introduced by assuming that the rate of sand transport remains constant and is proportional to the speed of the motor driving the belt. On the typical belt conveyor, that is used to transport the sand, slippage occurs between the drive roller and the belt which prevents the motor speed of the driven roller from providing an accurate indication of sand layer velocity. If this is a problem the sand layer velocity may be measured by monitoring actual sand layer or belt speed, specifically by measuring the angular velocity of an idle roller driven by the belt. The apparatus of this invention also uses a signal processing unit to continually calculate the required water addition that will provide the sand with a computed water content that represents the desired water content at some later stage. The later stage is usually when sand is withdrawn from the mixer and put in a casting mold. The signal processing unit uses at least the electrical resistance of the sand to gauge its moisture content and can be further programmed to include sand temperature and sand composition parameters in the calculation of sand moisture content. Another water addition value is then calculated, using the sand temperature, to determine an amount of additional sand moisture that will allow for evaporative losses between the time of resistance sensing and the final use of the sand in the casting mold and provide additional moisture content to the sand as the sand temperature increases. A higher moisture content is necessary at higher sand temperatures to give the sand proper molding properties. In order to increase the flexibility of control, the signal processing unit can be a programmable microprocessor for storing empirical coefficients and constants that refine the calculation of sand moisture content and water addition requirements. Finally, the addition of water to the sand is controlled by a valve having multiple positioning capability and which, in response to a signal representing the water addition value, will regulate the flow rate accordingly. The valve may be calibrated to fully position itself in response to an appropriate signal from the signal processing unit or a flow monitor may be used in conjunction with the valve and the valve repetitively incremented or decremented until the measured flow rate matches the water input value. The invention will be described in more detail, by way of example, with reference to the accompanying drawings, in which: FIG. 1 is a schematic diagram of an apparatus arranged in accordance with this invention. FIG. 2 is an isometric view looking at a section of a conveyor shown schematically in FIG. 1. FIGS 3 a and 3 b make up a flow chart showing an algorithm for the computations performed by the signal processing unit. A sand and mixing system arranged in accordance with this invention is shown schematically in FIG. 1. Sand is emptied from a hopper 12 onto a conveyor 14 and emptied into a mixer 16. Water is added to the mixture in a quantity regulated by a signal processing unit 18. The conveyor 14 and sand hopper 12 cooperate to deposit and transfer a uniform layer of sand 15 along the conveyor and into mixer 16. A supply of foundry sand is maintained in the hopper 12. Sand from hopper 12 is channeled through an opening 20 at the bottom of the hopper and directed onto a belt 22. Belt 22 is driven in direction A by frictional engagement with a head roller 24. A variable speed motor 25 drives head roller 24 through an appropriate gearing mechanism. Belt 22 is continuous and loops around head roller 24 and tail roller 26, with both rollers acting in opposition to maintain a desired amount of tension on the belt. As the belt moves in direction A, sand is carried away from opening 20 and under a striker edge 28. Striker edge 28 maintains sand layer 15 at a depth of 42 mm. As sand layer 15 advances over head roller 24, it drops off belt 22 and into mixer 16. Mixer 16 collects sand from the belt, mixes water with the sand to adjust its moisture content and allows sand to be withdrawn at a controlled rate for use in molds or forms. In simplified form the mixer consists of a containment vessel 30, a nozzle 32 through which water is directed into the mixer and a wheel and plough assembly 34 for mixing the sand and water. Sand is withdrawn through an opening 36 at one end of the mixer. A movable door assembly 38 regulates the withdrawal of the sand and water mixture from the hopper, with the withdrawal of sand being intermittent or continuous. A motor assembly (not shown) drives muller wheels 34 as water from a high pressure supply (not shown) is piped to nozzle 32 by a conduit 52 and directed into the mixer at a volumetric rate determined by the hereinafter described signal processing unit. Signal processing unit 18 has three basic functions: receiving measurments of the physical properties of sand entering the mixture; using these physical properties to calculate the necessary water addition to the mixer to achieve a desired sand moisture content; and delivering a control signal for regulating the addition of water to the mixer, so that water is supplied in the required amount. The signal processing unit monitors and controls the sand moisture content through a series of electrical signals, These signals are generated or received by sensors and electro-mechanical control devices located about the system. Signals indicative of the sand properties are obtained from sensors 40 that measure the electrical resistance of the sand and sensors 42 that measure sand temperature. FIG. 2 shows a section 200 of conveyor 14 over which sensors 40 and 42 are located. Conveyor section 200 consists of side members 202 and 204 which are welded together about a support member 206 to define a conveyor channel. A segment 208 of belt 22 slides on top of support plate 206 and extends across support plate 206 to about the edges of side plates 202 and 204. A sand layer 210 rests on top of belt 208 for movement therewith. The width of the sand layer is controlled by side plates 202 and 204, which maintain the sand layer at a relatively uniform width of 940 mm. A support frame 212, attached to the outside of side plates 202 and 204, spans the top of sand layer 210. Sensors 40 consist of two rectangular steel plates 214, 216 which are suspended from support frame 212 and extend approximately 255 mm into sand layer 210. Plates 214 and 216 are spaced 150 mm apart and have a width of 280 mm. A set of lateral supports 218 and 220 prevent transverse movement of plates 214 and 216 respectively. Each support 218, 220 is welded to an outer face of its associated plate, outer being taken to mean away from the center of the sand layer, and an upper corner of support frame 212. A power supply cable 222 is conductingly attached to the top edge of plate 214. A power output cable 224 is conductingly attached to the top edge of plate 216. The opposite ends of power cables 222 and 224 are connected to signal processing unit 18 and used, in a manner hereinafter described to establish an electrical circuit across the section of sand layer 210 between plates 214 and 216. Frame 212 is made of a nonconductive material such as wood or plastic to prevent the frame from shorting plates 214 and 216. Ahead of frame 212 a support structure 226 is attached to the outsides of side plates 202 and 204 and suspends sensors 42, over the sand layer. Sensors 42 comprise a set of three contact thermocouples 228, 230, 232. A flange 235 is positioned parallel to the sand layer and has three thermocouples secured thereto. Flange 235 is part of folded plate 234 which extends upward and is attached to the top of support structure 226. A backing plate 236 extends downward from the top of support structure 226 to stiffen support plate 234. Frame 212 and structure 226 are spaced close together so than sensors 40 and 42 are separated by less than the width of belt segment 208. A pair of stabilizer bars 238 and 240 extend from opposite sides of frame 212 and to opposite sides of plate 234. The stabilizer bars reduce deflection of the thermocouples under the drag loading of the passing sand layer. The probe ends of thermocouples 228, 230 and 232 are shown by dashed lines 242, 244 and 246, respectively. As shown by the drawings, these probe ends have different lengths so that they extend to different depths within the sand layer. A cable and conduit arrangement 248 connects the thermocouples with the signal processing unit 18. A sensor, positioned adjacent tail roller 26, measure the speed of the sand layer by monitoring the belt speed. This sensor consists of a proximity switch 44 located slightly above tail roller 26 to sense the passing of a probe 46 located on the periphery of tail roller 26. Therefore, revolutions of the tail roller which has a diameter of 460 mm are monitored to obtain a belt speed input. Monitoring the revolutions of tail roller 26 provides an accurate measurement of the belt speed since there is negligible slip between belt 22 and tail roller 26. A signal indicating the time for one revolution of the tail roller is obtained from proximity switch 44 and received by signal processing 18. Signal processing unit 18 also monitors the flow rate of water through conduit 52. A turbine type flow meter 54 positioned across conduit 52 sends a electrical signal indicative of the flow rate to signal processing unit 18. Signal processing 18, in a manner hereinafter described, generates a water control signal indicating whether flow to nozzle 32 should be increased or decreased. A control valve 56 is positioned across conduit 52 and receives thee water control signal. Control valve 56 is a solenoid operated electromechanical flow control valve. Looking in more detail at the signal processing unit, this can consist of any electronic data processing system that is capable of receiving electronic signals from the sensors and sending electronic signals to the control device. In this embodiment the signal processing unit consists of a standardized industrial controller 300 that interfaces with an operator panel 302. Controller 300 is a PLC 2/30 made by Allen Bradley. A series of input/output modules are included with the controller for converting and scaling analog signals that enter the controller into digital form and digital signals leaving the controller into analog form. The controller 300 has a remote power supply 304 for providing the necessary power for the sensors and control devices. In particular, controller 300 delivers a 6.57 volt supply to the conductive plates and uses a 0-20 millamp sensor to measure the current between the plates of sensor 40. Electrical signals from flow recorder 54, motor 25, theremocouples 42 and proximity switch 44 are also received by controller 300. The signals are processed within the controller which generates and sends the water output signal to control valve 56. Controller 300 executes a set of program steps, as hereinafter described, to generate the signal for control valve 56. In addition, controller 300 performs a series of data checks on the signals from the various signals. The controller receives additional input for performing the calculations and transmits data check information to control panel 302. Control panel 302 contiains a series of warning lights 306 and a thumbwheel control 308. When one of the signals, checked by controller 300, is out of tolerance, a corresponding warning light on control panel 302 is energized. The thumbwheel control 308 is positioned by the operator to send an digital signal to the controller that ultimately controls the moisture content of the sand in the mixer. The program steps or algorithim executed by controller 300 are set forth in flow chart form in FIGS. 3a and 3b. Acronyms for the various input and output signals, which appear throughout the specification and flow chart have the followig definitions: BP = signal indicating that motor 25 is running THR = thermocouple signal representing average sand temperature in degrees Fahrenheit PS = signal indicating input voltage to plates 40 PC = signal corresponding to output current from sensor 40 in milliamperes FR = flow rate of water input from meter 54 PX = input from proximity switch which is equal to the time in seconds for each revolution of tail roller 26 SMC = value obtained from thumbwheel which is scaled to equal 100 times the selected moisture content percentage CVS = signal to control valve. The algorithim begins with step 100. In step 101, BT, which is used to monitor the belt operation, is assigned a value of zero. At step 102, BP is read to determine if motor 25 is running and more generally if the system is on. An input module of controller 300 assigns BP a value of zero when the belt power is off and a value greater than zero when belt power is on. Step 103 checks whether the power is being supplied to the belt. If not, BT is again initialized to zero in step 104. Decision step 105 transfers the sequence to steps 106 if BT is not greater than zero. Step 106 uses an appropriate timing device to delay the program for five seconds and generates a signal for energizing a warning light in step 206. The warning light remains lit during the five second delay period to indicate that the belt is not running. The five second interval is used at this point to give the belt and sand layer enough time to reach steady state after the system is initially turned on. After five seconds BT is assigned a value of one in statement 107 and the program returns to 102 to again check if the belt is running. Once the belt has run for at least five seconds, BT retains a value grater than 1 and the program goes from step 105 to step 108. Sensor inputs THR, PS, FR, PX and DMC are read in step 108. The sensor inputs are then checked in the succeeding series of steps for out of tolerance values. In step 109, THR, is checked to make sure the sand input temperature is between 60°F (15.5°C) and 170°F (77°C). PS is checked in step 112 for minimum and maximum values of 6 and 7 volts, respectively. The amperage output value, PC, is checked in step 116 for a reading in the range of 1.6 to 16 milliamps. Flow recorder input FR is checked in step 120 for a value of 0 and 60 US gallons (227 litres) per minute. Finally, SMC is checked to see if it is between 110 and 500, which represents a moisture content between 1.1% and 5.0%. If any of inputs THR, PS, PC, FR or SMC are out of tolerance, then steps 110, 114, 118, 122 or 126, respectively, will energize an appropriate warning light in light set 206. Regardless of errors in the input, the program continues onto step 128. Step 128 uses an empirically derived equation to calculate the moisture content of the sand on the belt, MCB. This equation was empirically derived by sampling the moisture content of sand passing between the plates and plotting the moisture content as a function of the resistance across the plates. The coefficient 12.5 and the constant 55 were used to define a linear function that would approximate the moisture resistance curve. Thus, a similar approach can be used to derive suitable linear coeffients and constants for systems that do not match the belt and sensor geometry of the system described herein. Furthermore, the linear function was used in this embodiment for the sake of simplicity; however, the accuracy of the moisture content calculation may be improved in other applications by the use of a higher order, curve fitting equation. In addition, resistance is influenced by the sand composition and temperature. Therefore, a more general sand moisture equation could be derived having factors or variables for different types of sand and variations in sand temperature. Inclusion of such variables in the equation of step 128 were not necessary for this preferred embodiment since the sand used herein is ordinary foundry green sand and the sand usually falls in a range of between 80°F (27°C) and 160°F (71°C). Another emperically derived equation, set forth in step 130, computes the additional moisture content, AMC, that is necessary to compensate for evaporative losses and provide suitable molding properties at the measured temperature. Again this relationship is emperically derived and based on the specific conveyor-mixer arrangement of this embodiment which allows about 10 minutes to elapse between the time that the sand properties are measured and the sand is finally used in the mold. The basic form of the equation in step 130 is a well known relationship for adjusting sand moisture content with temperature to obtain suitable molding properties. It is only the constant, 50 and the coefficient of 1/100 that were adjusted to provide suitable moisture content compensation for the system herein described. In step 132 the desired flow rate, DF, is calculated by subtracting MCB and AMC from the selected moisture content of the sand, SMC, and dividing the sum by PX to obtain a rate. The coefficient 1.2 in step 132 is based on the geometry of the system herein described and contains the necessary volume and rate factors for converting the moisture content percentage and belt timing values into a gallons per minute value. In step 134, the desired flow rate is compared with the actual flow rate. If the desired flow rate is less than the actual flow rate, the routine goes to step 136 which decreases the digital count for the control valve signal, CVS. If the desired flow rate is greater than the actual flow rate, the routine goes to step 138 wherein the digital count for the control valve is increased. One of the hereinbefore described modules scales the value of CVS such that a digital value of 200 will generate a signal for fully closing control valve 56 and a digital value of one thousand will generate a signal that fully opens control valve 56. In step 140, the routine is delayed for a 100 milliseconds by a suitable timing device before returning back to step 102 and continuing the loop. The program then loops from step 140 to step 102 to check that the belt remains running. The delay of 100 milliseconds can be extended for other applications if hunting of the flow control valve becomes a problem. The flow chart of FIGS 3a and 3b describes the operation of the program in a general way which can be converted to a machine language and implemented by those skilled in the art. In addition, this description has set forth a specific configuration for the mixer, conveyor and control apparatus. This specific arrangement includes structural details, control system details and operating parameters that may be varied in order to tailor the system of this invention to other applications. For instance, it may be desirable to have the sensed parameters recorded for later retrieval and review. Furthermore, it may be advantageous to replace the control board with a CRT terminal which could display all input and output values.

Claims: Apparatus for measuring the moisture content of sand, comprising a conveyor (14) for transporting a layer (15) of the sand, a pair of electrode plates (40) lying in spaced, parallel planes parallel to the direction of transport of the layer of sand and, in use, dipping into that layer, and means (300) for measuring the resistance between the electrode plates (40) to determine the moisture content of the sand passing on the conveyor, characterised in that at least ten percent of the transported sand passes between the electrode plates (40), in that the dimensions of the plates (40) are such (e.g. a width of 280 mm) that the resistance of a relatively large volume of sand is measured, and in that the plates (40) are in fixed positions to provide for a continuous resistance measurement as the sand is carried between the plates by the conveyor (14) Apparatus according to claim 1, comprising means (28) for regulating the depth of the sand layer (15) on the conveyor (14) to a constant depth. Apparatus according to claim 1 or 2, characterised in that the plates (40) dip into the sand layer (15) for at least half the depth of the layer. Apparatus for controlling the moisture content of sand, according to any of claims 1 to 3, comprising means (42300) for measuring the temperature of the sand layer (15), means (44.46) for measuring the transport velocity of the sand layer, a signal processing unit (300) responsive to the calculated moisture content, a desired moisture content value, the measured temperature and transport velocity to calculate a water addition value, and means (56) responsive to that value to control the rate of supply of water to a mixer (14) for mixing added water into the sand. Apparatus according to claim 4, characterised by a device (308) for operator adjustment of the desired moisture content value. Apparatus according to claim 4 or 5, characterised in that the temperature measuring means (42,300) comprise a plurality of sensors (228,230,232) spaced across the width of the sand layer (15). Apparatus according to claim 4,5 or 6, characterised in that the temperature measurement means (42,300) comprise a plurality of sensors (228,230,232) dipping at different depths into the sand layer. Apparatus according to any of claims 4 to 7, characterised in that the temperature measurement means (42,300) comprise a plurality of thermocouples (228,230,232). Apparatus according to any of claims 4 to 8, characterised in that the conveyor (14) is a belt conveyor with a belt (22) extending around driving and non-driving rollers (24,26), and in that the means for measuring the transport velocity (44,46) measure the angular velocity of the non-driving roller (26). Apparatus according to any of claims 4 to 9, characterised in that the temperature measurement means (42,300) are spaced in the direction of sand transport from the conductive members (40) by a distance no greater than the width of the sand layer (15).

Inventors: MITCHELL, WADE STEVEN
Applicants: DEERE & COMPANY
Application year: 1987
Main classification: B22C5
IPC codes: B22C5, G01N27