GB2236876A - Control of the manufacture of plaster board - Google Patents

Abstract

To control the manufacture of plasterboard the supervisor enters required board parameters and production rate into a central processor. The processor senses the ratio of liquid raw materials to solid raw materials (AWAT) in a mixer and compares AWAT to a calculated setpoint value (SWAT). The set point value is adjusted in accordance with the difference between AWAT and SWAT. The height of a slurry dam behind an extruder on the boardline is then sensed and compared with a set point value (SDAM). If the sensed value (ADAM) differs from the set point value (SDAM) the setting belt speed (ABEL) is adjusted. The adjusted belt speed is then compared to the desired production rate (SBEL) and the raw materials feed rates varied to compensate for the difference.

Description

CONTROL SYSTEM AND METHOD FOR THE MANUFACTURE OF PLASTER BQARD This

invention relates to the manufacture of plaster board, and in particular to the control of the manufacturing process for optimisation of quality and resources.

In the plasterboard manufacturing process, raw =rponents are fed to a mixer. The solid raw materials are calcium sulphatehemihydrate and any additives required for the particular board being made. The liquid raw materials are process water, lignosulphonate solution, which is a water demand reducer, and a foaming solution. The foam is mixed in a foamer and includes water, air and a foaming agent.

From the mixer, the slurry of raw materials is released onto a sheet of facing paper and passed through an extruder. Before the extruder the edges of the paper are scored and folded upwards to provide side walls. A dam of slurry builds up in front of the extruder. Just before the extruder an upper layer of paper is laid down and adheres to the slurry and to the inwardly t urn ed sides of the lower paper layer. After the extruder, the slurry, sandwiched between the paper layers, passes onto an endless belt.

The board is then allowed to set as it travels along the boardline. Setting takes place of over about 3 to 6 minutes after which the board is scored and cut into lengths for drying. Drying typically takes place in a nultideck dryer over a period of about 1 hour. After drying the board may be divided into shorter lengths as desired.

In this process, it is essential to ensure that the formulation of the slurry, the delivery of the slurry onto the setting belt and the drying conditions for the formed board are correct to produce a high quality product.

Furthermore, changing over from production of one board type to another requires that the production line be stopped for periods of up to one hour while belt speeds are adjusted, slurry compositions altered and dryer times and temperatures changed. Each change in board type involves the line being shut down for up to an hour. As the line operates at speeds of around 50-60 metres per minute the loss in production is considerable.

The present invention aims to control the production of plasterboard to fulfil the requirements noted above and, to overcome the abovementioned problems, and accordingly provides a method of controlling the manufacture of plasterboard in which a slurry of raw materials from a reservoir passes to a setting belt, the method comprising the steps of selecting a desired belt speed and board composition, sensing the height of a slurry dam on the boardline, comparing the sensed height with a setpoint height and adjusting a parameter affecting the dam height in accordance with the deviation between the sensed and setpoint heights.

Preferably the parameter affecting the dam height is the setting belt speed and the method further comprises comparing the setting belt speed with a setpoint belt speed and adjusting the feed rates of raw materials to the reservoir to compensate for the difference between the setting belt speed and the setting belt setpoint. The advantage of adjusting the belt speed is that the belt motor can react to instructions to change speed almost instantaneously whereas other parameters such as raw material feeds can take up to 30 seconds to react.

By a system of interactive control loops the method of the invention may optimise operating conditions for a given board fo=lation. Preferably the system is controlled by a central processor into which the supervisor enters the desired formulation and production rate. The processor then adjusts the variables in accordance with the method of the invention.

Preferably, the central processor can transmit to local parameter controllers details of a fresh set of set point values indicative of a change in desired board parameters. In the case of a change in board width the method further comprises stopping the board production, adjusting the width of board to be produced, restarting the board production at slow speed and resuming the set point conditions on sensing that board edges are being formed correctly.

The invention also provides apparatus for controlling the manufacture of plasterboard in a boardline comprising a slurry reservoir for raw materials, a setting belt arranged to receive the slurry passed from the reservoir and feeds for feeding individual materials into the reservoir, the apparatus rising means for sensing the height of a slurry dam on the boardline, means for comparing the sensed height with a set point height, and means for adjusting a parameter affecting the dam height in accordance with the deviation between the sensed and setpoint heights.

Preferably the adjusting means comprises means for adjusting the setting belt speed, the apparatus further comprising means for comparing the setting belt speed with a set point belt speed, and means for adjusting the feed rates of raw material to the reservoir to compensate for the difference between the setting belt speed and the set point setting belt speed.

The invention also provides a method of controlling the manufacture of plasterboard in which a slurry of raw material is passed from a reservoir to a setting belt, the method comprising the steps of selecting a desired belt speed and board composition, sensing at least one parameter dependent on the composition of the slurry, comparing the sensed parameter value with a setpoint parameter value, and adjusting a setpoint value of a component of the slurry in accordance with the deviation between the sensed and setpoint parameter values to adjust the sensed parameter value to the setpoint parameter value.

In a further aspect of the invention there is provided apparatus for controlling the manufacture of plasterboard in a boardline comprising a slurry reservoir for raw materials, a setting belt arranged to receive the slurry from the reservoir and feeds for feeding individual materials into the reservoir, the apparatus comprising means for sensing at least one parameter dependent on the slurry csition, means for comparing the sensed parameter value with a setpoint parameter value, and mans for adjusting a setpoint value of a component of the slurry in accordance with the deviation between the sensed and setpoint parameter values to adjust the sensed parameter value to the setpoint parameter value.

A preferred embodiment of the method and apparatus of the invention will now be described, by way of example, with reference to the accompanying drawings, in which:

line; invention.

Figure 1 is a schematic view of a plaster board manufacturing Figure 2 is a block diagram of the control apparatus; and Figure 3 is a flow diagram of the control process of the In Figure 1 the raw components are introduced into a mixer 1 by feeds, tyn of which are shown at 3 and 5. Sensors (not shown) monitor the amount of each of the raw materials introduced into the mixer. The mixer has an exit 7 for egress of slurry onto lining paper 9 fed from a roller 11. Once the slurry has been laid down a dam of slurry builds up in front of an extruder 13. The extruder regulates the thickness of the plasterboard and may be raised and lowered as desired. Before the lower paper layer 9 reaches the extruder its edges are scored (at 10) and bent upwards to form the sides of the board. A capacitative sensor 14 measures the height of the slurry d&n. A second, upper layer of lining paper 15 is applied from a roller 17 before the extruder and is glued on the upper inturned edges of the lower lining paper. After the extruder the board is conveyed on a setting belt 19 until the slurry sets, after which it - 5 is cut and fed into a dryer. The dryer my be a multilayer dryer in which, for example, twelve parallel lines of board are dried, the lines being separated to allow drying air to pass over each surface of each board in the drier.

Figure 2 shows the main elements of the control system embodying the invention. overall control is from the control computer 30 which can dictate operating parameters to each local control unit.

The type of plasterboard produced by the process, and its quality, depends on three principal factors: the composition of the slurry; the dam height, that is the height of slurry behind the extruder; and the setting belt speed.

Each of these three factors has its own control loop or loops which the central computer oversees. The loops interact to ensure that the amount and proportions of raw materials fed to the mixer is correct for the type of board being produced and that there is sufficient slurry leaving the mixer for the production rate, which is dictated by the setting belt speed and the board type.

Thus in Figure 2 a speed sensor 32 is mounted on the setting belt drive motor and sends speed signals of actual belt speed ABEL to the computer. The central computer 30 can send set point belt speeds SBEL to a microprocessor control unit 34 for the setting belt motor.

Similarly a sensor 14 is mounted in the extruder 19 to sense actual dam height ADAM and these height signals are sent back to the central computer.

The amount of raw materials supplied by each of the feeds is also measured, shown at 38, and corresponding signals transmitted back to the central computer 30. In turn the computer can transmit set point raw material levels to the local control units 40 of the raw material feeds. The set points may either be determined by the process supervisor in accordance with the board to be produced and the desired production rate or recalculated by the computer in accordance with the other sensed conditions as will be described.

Sensors 44 are also munted in the dryer and the computer can dictate drying temperatures and feed through-speeds to the local dryer control 46.

The first control loop is the production rate. This rate is determined by the setting belt speed. The operator enters a desired, or set point, belt speed, SBEL from the control panel and also enters estimated raw material set points for the board to be produced at this belt speed. The material set points will be referred to as SMT.

The belt drive is provided with a speed sensor that passes a signal ABEL to the computer indicating the actual belt speed. The belt speed controller can compare ABEL with SBEL and make necessary adjustments to the belt speed.

The second control loop is the water gauge. It is important that this is maintained at a constant level for the purposes of quality control, cost control and drying efficiency. The water input to the slurry comprises three separate sources; an aqueous foam, lignosulphonate water and process water which provides the balance. The target, or setpoint, water gauge SWAT is entered from the central control either manually or by calculation from one of the other control parameters.

The raw materials which are fed to the mixer 1 are measured by conventional means and controlled using local dedicated loop controllers. These local loop controllers are subject to the main system control in the system hierarchy; that is, the main control can override the local microprocessors or controller.

The calcium sulphate-hemihydrate is measured by a Schenck weigh belt feeder which incorporates its own microprocessor based controller.

Other solid raw materials, which may be added in dependence on the type of board to be produced, are measured using loss-in-weight feeders incorporating their own microprocessors.

The three liquid feeds are measured using magf low meters and controlled using dedicated microprocessor-based loop controllers to adjust purp speeds or valve positions.

The weigh belt feeders, loss-in-weight feeders and the flow meters act to sense the amounts of materials entering the mixer as mentioned in the description of fig-ire 1. Of course, any other type of measuring devices way be used as is convenient.

Thus, the actual water gauge AWAT is dependent on the solid and liquid feed rates as follows ANAT = ALIQ ASOL where ASOL is the actual solid feed rate and ALIQ is the actual liquid rate.

The main system controller controls the value of AWAT by comparing AETAT with SWP.T and trimming the setpoint sent to the main water feed which has the effect of altering the proportion of liquid to solid in the raw materials.

In practice, each of the dedicated loops of the water gauge control operates continuously, whereas the set point comparison and revision by the main controller operates on a one second cycle.

The third control loop is the dam height. Whereas the production rate and the water gauge ensure that the feed rates of the various cnents of the slurry are constant and that the production targets are met, changes in trature, entrainment factors, splices from one paper reel to the next and other variables require that the dam size varies. If the rate of egress of slurry from the mixer is too high, excess slurry will weep at the edges through the fold over of the lining paper, destroying the adhesion between the top and bottom liners. A feed rate that is too low results in the edges of the board being empty.

The dam height is a secondary control as conveyor speed SBEL provides the primary control. The dam height ADAM is a measure of the height of slurry behind the extruder. The dam height may be varied either by adjusting the belt speed for a given feed rate or by varying the feed rates.

The action of the dam height control loop is superimposed on the conveyor speed setpoint SBEL. The range of the output of the dam height controller may be varied but is typically between +/- 0. 1 m/min and +/- 1. 0 m/min. Thus as the dam height ADAM varies from its setpoint SDAM, a control signal CDAM is generated which is proportional to the deviation from the setpoint. Thus, CDAM ADAM-SDAM.

The dam height ADAM is measured by a capacitance-type sensor which is incorporated into the main forming section and generates an output proportional to the dam height. This is a departure from conventional dam sensors which use on-off capacitance devices to indicate excessive dam heights.

Other control parameters may be introduced into the dam height control loop. For example, filters to eliminate the effects of minor variations, dead band, timer delays and conventional integral and derivative terms. The output of the dam height loop controller is mathematically treated by the central computer to provide the appropriate triuming value (typically +/- 0.75 m/min) which is then added to the belt speed set point originally entered by the plant supervisor to give an adjusted setpoint SBEL which is transmitted to the dedicated local belt speed controller. The overall effect of this loop is to maintain the darn size by trinning the belt speed.

t Figure 3 shows by way of a flow chart how the various control loops interact to provide an overall control for the system.

After the central computer has determined, at 100, whether the plant is running, it ces, at 102, whether the measured water gauge AWAT equals the pre-entered setpoint SWAT. If AWAT = SWAT then the dam height is examined.

If AWAT SWAT then the value of AWAT is altered at 104 by varying the amount of water introduced into the slurry. This is done by the main computer which calculates a new main water set point RGJN for the dedicated water controller based on the deviation between ANAT and SWAT. Once the new value of SMAIN has been transmitted to the local controller step 102 is repeated. The recalculation of SMAIN continues until AWAT = SWAT.

The control computer then compares the dam height to the setpoint dam height. Thus in step 106 the computer compares ADAM and SDAM. If the tjm values are equal the process moves on to step 110. If not, the belt speed setpoint SBEL is varied at step 106. The belt set point is adjusted as a function of the difference between the sensed dam height ADAM and the set point dam height SDAM.

The adjusted belt speed setpoint deternuned by the central computer is then transmitted to the local belt speed controller. Step 106 and, if necessary step 108, is repeated until the sensed dam height ADAM is equal to the setpoint dam height SDAM.

At the next step 110 the raw material feeds are trimmed to take account of changes in set points in the first two control loops. If no trim is required the control process is completed and the process holds for a predetermined delay of between 1 and 30 seconds.

It is possible that the effect of adjusting the belt speed setpoint SBEL to maintain the dam height SDAM is that SBEL deviates from the original speed selected by the operator to meet the required production rate. At step 112 the system perform a continuous 1 running average 1 calculation on the speed. At regular intervals, which might be between ten seconds and ten minutes and which typically is approximately three minutes, the system uses the deviation between the required speed and the running average to calculate adjustments to be made to the setpoints of selected raw materials. It is possible to use this deviation to provide adjustments for all of the raw materials or to apply adjustments to only selected items. The corrective control signals might be directly proportional to the deviation or might be subject to intermediate mathematical manipulation.

Thus, at step 114 the central computer calculates new raw material setpoints and transmits these to the dedicated control loops for the materials. Steps 112 and 114 are repeated until the average belt speed is correct and no setpoint changes are necessary. This step signals the end of the control process and the omputer waits for the predetermined delay at 116 before ret urn ing to step 100.

The water gauge control loop is dedicated to ensuring that whenever adjustments are made to the feedrates of the gypsum plaster and/or to the water-containing additives, the overall proportion of gypsum plaster to water is preserved. Thus as the dam controller adjusts the belt speed and belt speed controller adjusts the raw material feedrates, so the water gauge controller adjusts the setpoint to the main water feeder.

in addition to the optimisation of running conditions for a selected set of board parameters the process has advantages in switching between different board formulations, board widths and board thicknesses, as the system supervisor my change the operating parameters at the central control and the control program described with reference to Figure 3 will adjust the setpoints as is necessary. In addition the coirputer calculates the revised formulation for each of the set points together with revised speeds through and temperatures in the drying oven.

After selecting appropriate operating conditions the supervisor may direct the computer either to proceed or to abort the changeover. If the 'proceed, instruction is given the coirputer activates a further program which selects the appropriate changeover routine from four main prograrms, 1, 2, 3 and 4. The routine is selected according to the board currently being produced and the type of board to be produced. The programs perform the following functions:

Program 1. Intended for changeover when the plant is already off-line or when the changeover will necessitate the plant being stopped e.g. for a width change. The plant is restarted at a slow speed to enable the edges to be properly formed whilst generating the rdxLi= amount of waste. Once the edges are properly formed, the conputer oversees acceleration up to full speed.

Program 2. Intended for changeovers which do not involve a board type change e.g. changes in belt speed, board weights, water gauge etc. There are two versions of this routine, one being used for small changes e.g. speed changes of less than two metres per minute, the other for larger changes. For small changes, the computer initiates a step change at the wet end and changes dryer conditions at appropriate times i.e. imTediately if the change is in belt speed or after calculated delays if the change is in formulation.

Program 3. intended for changeovers to a new board type which is run at a higher speed than the board currently being made e.g. for thinner board. Such changeovers would previously require the plant to be stopped for up to an hour whilst the dryer is emptied.

when changing board types the routine produces a buffer board of the new type for typi-callY ten to fifteen minutes. once it has started to make the buffer board, the computer begins to alter the fonnilation to the normal formulation for the new board but at the speed of the old board. Upon ccupletion of this raTrp, the new board is made at the old (slower) speed until it is safe to go to full productions speed. Throughout this time, dedicated sub-routines ensure that all of the board is properly dried by trimming dryer temperatures. The use of this changeover routine does not result in any losses in dry board.

The final routine is intended for changeovers involving reduced production speeds e.g. for thicker board. It is similar to the previous routine and but operates in reverse. Again, the routine does not result in losses of dried board, and small amounts of waste material only are generated.

In existing board lines, each automatic changeover enables the machine to be run for 45 mins longer than would be the case with manually controlled systems. This represents an increase in weekly machine availability of 0. 45% per changeover made.

Moreover, the effect of the control process to change production without serious loss is that just-in-timel manufacturing techniques may be adopted. Such techniques allow special types of board to be manufactured as and when they are required. Thus, such boards need not be kept in stock reducing warehousing requirements and reducing the amount of board lost due to damage whilst in stock.

claim 1. A method of controlling the manufacture of plasterboard in which a slurry of raw materials f= a reservoir passes to a setting belt, the method corrprising the steps of selecting a desired belt speed and board composition, sensing the height of a slurry dam on the boardline, comparing the sensed height with a setpoint height and adjusting a parameter affecting the dam height in accordance with the deviation between the sensed and setpoint heights.

2. A method according to claim 1, wherein the parameter affecting thedarn height is the setting belt speed and the method further comprises comparing the setting belt speed with a setpoint belt speed and adjusting the feed rates of raw materials to the reservoir to corrpensate for the difference between the setting belt and the setting belt setpoint.

3. A method according to claim 1 or 2 wherein prior to sensing the dam height at least one parameter dependent on slurry c=position is sensed, the sensed parameter value is compared with a setpoint parameter value and a setpoint value of a corrponent of the slurry is adjusted in accordance with the deviation between the sensed and setpoint parameter values to adjust the sensed parameter value to the setpoint parameter value.

4. A method according to claim 1, 2 or 3 wherein the composition dependent parameter sensed is the ratio of water to solid raw materials in the slurry.

5. A method according to any of claims 1 or 4, wherein the composition dependent setpoint is adjusted by varying a setpoint controlling the amount of water adnitted into the slurry.

6. A method according to any of claims 1 to 5, wherein the setpoint belt speed is indicative of the desired production rate.

7. A method according to any of claims 1 to 6 wherein the feed rates of raw materials are measured by sensors prior to the admittance of the respective materials into the reservoir.

8. A method according to any preceding claim wherein the height of slurry in the dam is further controlled by adjustment of the raw material feed rates.

9. A method according to any preceding claim, wherein the respective values sensed are transmitted to a central processor and the adjusted setpoint values are calculated by the central processor and transmitted to respective local controllers.

10. A method according to claim 9 comprising the step of transmitting to respective local controllers a fresh set of setpoint values indicative of a change in desired board parameters.

11. A method according to claim 10, ccrprising stopping the board production, adjusting the width of board to be produced, restarting the board production at slow speed and resuming the setimint conditions on sensing that board edges are being formed correctly.

12. A method according to claim 10, c=prising effecting a step change in the set point values and adjusting formed board drying conditions.

13. A method according to claim 10, wherein the setpoints are changed for production of a thinner depth board, cmprising producing a buffer board at the new board thickness, gradually adjusting the amposition of the buffer board to the desired composition of the thinner board until the desired csition is reached, holding the production at the desired sition for a predetermined period, and increasing the belt speed to that required for the new board thickness.

14. A method according to claim 10, wherein the setpoints are changed for production of a thicker board, cmprising producing a buffer board at the original board thickness, adjusting the sition of the buffer board to that of the thicker board, and decreasing the setpoint belt speed in accordance with the increased thickness board.

15. Apparatus for controlling the manufacture of plasterboard in a boardline comprising a slurry reservoir for raw materials, a setting belt arranged to receive the slurry passed from the reservoir and feeds for feeding individual materials into the reservoir, the apparatus comprising means for sensing the height of a slurry dam on the boardline, means for c=paring the sensed height with a set point height, and means for adjusting a parameter affecting the dam height in accordance with the deviation between the sensed and setpoint heights.

16. Apparatus according to claim 15 wherein the adjusting rreans rises iTeans for adjusting the setting belt speed, the apparatus further corrprising means for ccniparing the setting belt speed with a set point belt speed and means for adjusting the feed rates of raw material to the reservoir to cxmpensate for the difference between the setting belt speed and the set point setting belt speed.

17. Apparatus according to claim 15 or 16 couprising sensor means for sensing at least one parameter dependent on the slurry csition, means for cing the sensed parameter value with a setpoint parameter value, and means for adjusting a setpoint value of a cnent of the slurry in accordance with the deviation between the sensed and setpoint parameter values to adjust the sensed parameter value to the setpoint parameter value, 18. A plaster boardline coffprising the control apparatus of claim 15, 16 or 17.

19. Plasterboard manufactured under the control of the process of any of claims 1 to 14.

20. A method of controlling the manufacture of plasterboard in which a slurry of raw material is passed from a reservoir to a setting belt, the method rising the steps of selecting a desired belt speed and board =position, sensing at least one parameter dependent on the composition of the slurry, comparing the sensed parameter value with a setpoint parameter value, and adjusting a setpoint value of a component of the slurry in accordance with the deviation between the sensed and setpoint parameter values to adjust the sensed parameter value to the setpoint parameter value.

21. Apparatus for controlling the manufacture of plasterboard in a boardline rising a slurry reservoir for raw materials, a setting belt arranged to receive the slurry passed from the reservoir and feeds for feeding individual materials into the reservoir, the apparatus comprising me= for sensing at least one parameter dependent on the slurry composition, neans for comparing the sensed parameter value with a setpoint parameter value, and means for adjusting a setpoint value of acomponent of the slurry in accordance with the deviation between the sensed and setpoint parameter values to adjust the sensed parameter value to the setpoint parameter value.

22. A method of controlling the manufacture of plasterboard substantially as described herein with reference to Figares 2 and 3 of the accompanying drawings.

23. Apparatus for controlling the manufacture of plasterboard substantially as herein described with reference to the accompanying drawings.

Published 1991 at The Patent Office. State House. 66/71 High Holborn IA)ndonWCIR4TP. Further copies maybe obtained from Sales Branch. Unit 6. Nine Mile Point. Cwmrelinfach. Cross Keys. Newport. Nl 7RZ. Printed by Multiplex techniques ltd. St Mary Cray. Kent