METHOD OF AUTOMATIC PARTICLE ANALYSIS AND MEANS FOR PERFORMING THE ANALYSIS

Abstract: The invention relates to a method and means for automatic analysis for determining the size distribution of particles and deviation from desired shape and colour. The method includes collection of particle samples and generation of a particle curtain in monolayer form. It is formed by taking particles through a silo whose distance (a) to a vibrating plate positioned below has a length relative to the distance (b) between the outer edge of the plate and the centre line of the silo that is large enough for the particles flowing out of the silo and down onto the plate and out over its edge to form an angle alpha with the horizontal plane. The angle alpha is 95 - 50 % of the sliding angle of the particulate material. The particle curtain is lit up and the silhouette of the particles therein is recorded and analyzed and presented in at least one place. The means includes sampler (1) plus silo (3) with at least one level sensor (4) to record the level of particles in the silo (3) and to give a signal to sampler (1). The silo (3) has a vertically displaceable extension (6) at its outlet opening. The lower part of the extension (6) is at a distance (a) from a vibrating plate (8).

Description: Method of automatic particle analysis and means for performing the analysis The present invention relates to a method for automatic analysis to determine particle size distribution and devia¬ tion from desired shape and colour. The method includes collection of particle samples and generation of a particle curtain in monolayer form, lighting of the latter and taking pictures that are analyzed. The invention also relates to means, particle feeding system, to carry out the method. This includes means for generating a particle curtain in monolayer form. During production of particulate material, or in processes where such material shall be added in at least one process stage, it is important to be able to control the process, so that the desired size distribution of the particle shaped material is obtained. However, the shape of the particles can also be important for the quality of the product, there¬ fore it is desirable to know the particles deviation from desired shape and colour so that the process can be con¬ trolled with regard to this criteria also. It has long been desired, in the fertilizer industry, to have reliable information about the end product size dis¬ tribution and particle shape, as optimal values for these parameters is of importance both from a purely economical point of view and when using the product, e.g. when spread¬ ing the produced prills or granules. Furthermore a process will be most economical if it gives a product with narrow sieve span, without having to sieve away large fractions that have to be run in return. Several analysis apparatus and measuring techniques are already available, and are used to solve aforesaid problem, however their applicability is usually limited to very special processes. Thus a particle analysis apparatus is known from U.S. patent number 4.497.576, where a silhouette projection method is used. The apparatus also includes use of parallel laser beams directed through a sample of par¬ ticles, and means for recording the light which has passed through. This recording is then analyzed to reveal the par¬ ticle size distribution in the aforesaid sample. A series of conditions which have to be satisfied for the measure¬ ments to be representative is listed in the patent, but it doesn't clearly appear how these conditions should be real¬ ized. The particles to be analyzed, are transported on a conveyor belt and fall from it in front of a light source and down onto the next conveyor belt for return to the pro¬ cess. One condition which is stated is that the particles falling from the conveyor belt must form a monolayer of particles and that they should fall at the same speed. How such a monolayer is obtained practically is not stated, and the aforecited means appears to be badly suited for the application. Furthermore from DE number 27 41321 means for determining particle size distribution in a falling particle stream by recording and analysis of video pictures is known. The par¬ ticles flow out of an extended slot in a silo and thereby form a curtain of particles passing a video recorder equipped with a heat picture camera. In addition to the size distribution, the means registers whether the particles deviate strongly from a spherical shape, as the particles heat content is recorded. The patent does neither state how to take representative samples, nor whether special measures are necessary for the analyzed particle curtain to be rep¬ resentative. It is stated that fine dust does not substan¬ tially disturb the result of the analysis. The means is primarily used for analysis of the size distribution of various additives for asphalt. Although the aforecited patents give information which clarify the problem of particle analysis to a certain ex¬ tent, they do not give practical solutions to problems of controlling fertilizer granulation/prilling through particle analysis, and that was what the inventor primarily had to find a solution to. The object of the present invention was to develop a method and means which could give current information on particles deviation from desired shape, alternatively colour or size, for thereby to be able to obtain more even product quality and faster response to operational changes in the process. The first condition to obtain good control of a particula- tion process, for example fertilizer prilling, is that, at any time, representative samples of the intermediate or end product can be taken. The inventors found that the problem could be solved in several ways by adaptations of conven¬ tional sampling systems. Accordingly a container with a slot for particle inlet, may be used. With such a system, samples could be taken by letting the containers slot open¬ ing traverse the stream of product particles on a conveyor belt or falling from such a belt. The slot opening must pass the whole cross section of the particle stream at a regular speed, and fast enough to avoid overfill of the sample con¬ tainer. In addition, it must be possible to completely empty it rapidly so that new samples can be taken. The traversing may for example, be carried out by help of double-acting compressed air cylinders. The next step in the analyzing process was to make the samples accessible for representative analysis, which one wished to get analyzed and presented shortly after the sample was taken. The solution to this problem will, to a certain extent, depend on the technique chosen to analyze the particle sample. Sieving and weighing was found to be too time consuming and unsuited for this application. How¬ ever, some type of picture representation of the particle curtain seemed interesting. The task was then to supply reproduceable and representative particle streams of the sample taken. Whether one chooses lighting of the particles by laser beams, infrared light or taking pictures using film/video camera or photography, it was found that obtain¬ ing a particle stream in form of a monolayer of particles, was essential. The means indicated for this in aforecited U.S. patent number 4.497, 576, could not be used. It was, among other things, very difficult to dimension the conveyor belt properly and set its speed to make sure that one ob¬ tained a monolayer of particles over the whole width of the conveyor belt. This apparatus assumes in addition that the particles free fall speed is known. The inventors chose then to feed the particles on to a vibrating plate to generate a monolayer of falling par¬ ticles. The results of the first tests were so promising that further development of the idea was initiated. It appeared that dosing the particles down on to the plate was a critical parameter. The problem was solved by using a silo whose outlet opening had to be placed in a certain, but adjustable, distance from the plate. Furthermore the dia- meter of the outlet opening had to be adapted to the par¬ ticles to be analyzed. A conventional silo could for that matter be used, but it appeared to be necessary to provide it with level sensors to measure the distance to the plate and the level of particles in the silo. The last mentioned level sensors could give impulse to the sampler, for example so that a more or less constant particle level was main¬ tained in the silo. The distance to the vibrating plate appeared to be critical to obtain supply of the right quan¬ tity of particles from the plate. Furthermore, the inventors found that the design of the plate was important to obtain a regular monolayer of particles supplied from it. A regular monolayer of particles was supplied all around the periphery of the plate adapted to the feed from the silo, by choosing a circular plate and adjusting amplitude and frequency. An additional parameter appeared under further testing, also to be determining for a good result. The products angle of inclination against the plate had to be kept below its slid¬ ing angle. The sliding angle for the type of product con¬ cerned had therefore to be determined, and it was 28° for the tested particle samples. The correct angle may be ob¬ tained in different ways or a combination of these. Accord¬ ingly the plate may be given a slightly conical shape, whereby the quantity of particles on the plate is reduced so that the residence time of the particles on the plate is also reduced. Experiments showed that the system functioned very well according to the plans when the angle of inclina¬ tion of the product against the horizontal plane was about 2/3 of its sliding angle. A particle feeding system built according to the above stated principles and by adapting the critical parameters to the products characteristics, par¬ ticularly the diameter and sliding angle of the particles, was found to be able to deliver a regular flow of particles in monolayer. Analysis of the particles in the monolayer could as already mentioned be carried out in several ways, but the inventors found it most advantageous to take pictures of the monolayer continuously or discontinuously with, for example, a video camera so that silhouette pictures of the particles was obtained. Thereby both their shape and size distribution could be registered. Special computer programmes for cal¬ culation of deviation from desired shape were developed. By measuring the circumference and area of individual parti¬ cles, their deviation from desired shape could be calculated and the particles size distribution in the production stream. Since sampling, generation of the particle curtain and analyzing the particles can be carried out continuously, the production parameters can be adjusted as a function of the results of the analysis. The special features of the invention are as defined in the attached patent claims. The invention will now be further explained in the following examples and figures. Fig. 1 shows a particle feeding apparatus according to the invention. Fig. 2 shows assembly of units used under the realization of the method according to the invention. The particle feeding apparatus shown in Fig. 1 includes a sampler 1 to fetch the particle samples at a suitable point in the process, for example a conveyor belt (not shown) . The sampler 1 can be a container with a lengthways slot opening. When a sample is taken, the sampler 1 is emptied directly into a silo 3, or the sample is sent to the silo via a pipe or a transport device 2. The silo 3 is equipped with a movable extension 6, at the outlet opening of the silo 3. Particles 7 are discharged from the silo 3 down onto a vibrating plate 8, and under performance a layer of par¬ ticles 7 will on the plate 8 form an angle oc. with the hori¬ zontal plane. The angle o is smaller than the sliding angle of the product (particles) to be analyzed. It may for example be only a few degrees smaller than the sliding angle, but to avoid a too sensitive system, an angle Λ that is 2/3 of the sliding angle is preferably used. The angle A may be set in several different ways, particularly by regulating the extension 6 to a distance a relative to the distance (b) from the outer edge of the plate 8 to the centre axis of the silo 3, or its cross section, which gives the desired value of the angle Λ. The silo 3 may be equipped with a distance sensor 5 for thereby to be able to regulate the distance a. Furthermore silo 3 has at least one level sensor 4. For example both a minimum and a maximum level in the silo 3 may be registered. Level sensor 4 will give a signal for sampling. Sampling device 1 can accordingly be connected to a double acting cylinder that, during sampling, lets container 1 traverse the whole width of a particle stream being on a conveyor belt or falling from such a belt. Particles will then be caught in a slot in the container and with the right choice of speed on the container 7 during sampling, it will not be overfilled, at the same time as one is guaranteed a repre¬ sentative sample of the production stream. The silo 3 may also be divided in several chambers with the help of ver¬ tical partitions. The plate 8 may vibrate in known manner, and both the fre¬ quency and the amplitude may be regulated. By regulating the distance a so that c is smaller than the sliding angle and by vibrating the plate 8, the particles will run out over its edge. Preferably a circular plate 8 is used, and certain sectors of it may be blinded off so that particles only run out over parts of the periphery of the plate 8. The plate 8 may be made slightly conical, but such that its conicity is smaller than the sliding angle. By adjusting the vibrators amplitude and/or frequency one can easily make sure that the particles fall down from the plate in a mono- layer 10 of particles. The particle stream or particle cur¬ tain 10 may then be lit up by a light source 9. The light source 9 may be a normal lamp, a set of laser beams or a flash which lights at signal. Fig. 2 shows the particle feeding system according to Fig.l connected to means for taking pictures of the particle cur¬ tain 10 as well as means for "on line" analysis and data processing, whereby one gets a complete plant for automatic particle analysis. The unit 11 may be a film or video camera, but also a re¬ cording unit for penetrating light, for example laser beams. A video camera taking photograph all the time is preferably used, but if the light source is a flash the photographs will be recorded only at each flash. The unit 12 is a pic¬ ture analyzer analyzing pictures continuously or discon- tinuously. This unit can include means giving signal 13 for the release of flash 9 or for picture taking by means of the unit 11 each time analysis of a picture is completed. The unit 11 may be used to photograph the silhouettes of particles in the particle curtain 10, but may also be used to differentiate between various colours or grey shades of the particles. The current video picture consists of 512 x 512 points (pic¬ ture element, PIXEL) . The number of PIXEL which are black, give thereby the area of each particle. The circumference is determined by a contour following routine. The picture analyzer 12, which may be integrated in a PC, contains the necessary computer programmes for reading and storage of pictures to enable measurement of area and circumference of each particle on the video pic¬ tures. The raw data from the picture analyzer 12 are then used for later data processing, for example in a PC 14. With the help of suitable data processing programmes, the raw data will be processed so that particle size distribution and various expression for the particles deviation from desired shape are obtained. The data from the unit 14 are then presented on at least one unit 15, which may be a printer or computer screen, and the result of the particle analysis is then transferred to the relevant part of the process for controlling the process towards optimal production and product quality. Data may of course also be stored for later study of relevant parts of the process. Example 1 This example shows production of a particle curtain in mono- layer form by means of an apparatus according to Fig. 1. Flow characteristics and sliding angle were first measured for the different types of products. Thereupon each type of product was one by one sent through the silo down onto a vibrating, circular plate. The particle level in the silo was kept more or less constant during the tests, by supply¬ ing new particles, and a silo opening with a size guaranteeing that even the largest particles or particle agglomerates could flow out, was used. A circular extension (unit 6 on Fig. 1) was provided around the silo opening, and the extension could be lifted and lowered so as to regulate distance a between the plates and the silo opening. The distance (a) was set in such a way that the inclination of the product towards the plane disc was roughly 2/3 of the sliding angle of the product. The vibrator was started, whereby the particles started to flow regularly over the periphery of the plate. By varying the vibrators frequency and/or amplitude it was made relatively easy to set the vibrator so that the particle curtain consisted of a mono- layer of particles. When the right setting for the vibrator was first found, the setting could be kept approximately constant for the same type of product under the whole test. When testing on several types of product, it was found that the inclination angle <X for the product against the hori¬ zontal plane, should be lying at least 5 % under its sliding angle, and preferably greater than 50 % of this. Adjusting the vibrator to obtain monolayer, was easiest for most types of product, when angle c was lying between 70-60 % of the sliding angle of the product. Vibrator adjustment and/or the extension 6 may, if desired, be controlled with the help of computer programmes so that the number of particles in the picture is kept approximately constant. Example 2 This example shows automatic particle analysis according to the invention and where results are compared with tradition¬ al sieving methods (laboratory sieving) of samples as well as deviation from desired shape. Calibration was done by placing a completely spherical ball with known diameter in front of the video camera. The dia¬ meter in millimeters was then read into the computer pro¬ gramme, the picture analyzer was subsequently tested on completely spherical particles of different sizes. Further¬ more the particles in the individual samples were in advance manually controlled to assess their deviation from spherical shape. Eight samples of about 2 kg prilled fertilizer were taken. Each sample was laboratory tested to assess particle size distribution, deviation from desired shape. The samples were then analyzed according to the invention, the particles being fed with the help of a particle feeding means accord¬ ing to Fig. 1, past a video camera that took pictures of the particles. The analysis showed that pictures which contained 10-20 particles took roughly 1 second to analyze. The ana¬ lysis time could however be considerably reduced. As soon as the processing of a picture was finished, a signal was given for a new picture to be taken. The results of the picture analysis (B) according to the invention, laboratory sieving (L) and deviation from desired shape is given in Table l, which shows particle size dis¬ tribution and the samples deviation from desired shape in percentage. The sieving analysis are in gram/100 grams. As it appears from the table, the laboratory sieving covers somewhat wider intervals (sieving categories) than the pic¬ ture analysis. TABLE 1 PARTICLE ANALYSIS As it appears in Table 1, there is very good accordance between the results of particle size distribution measured by laboratory sieving and by the method according to the invention. As far as analysis of deviation from spherical shape is concerned, it corresponds well with common judge¬ ment concerning good and poor product. However, the method according to invention gave a more accurate expression of the particles deviation from desired shape. Example 3 This example shows an investigation of granulated fertilizer particles. The studies were carried out in the same way as described in Example 1, but in the last example deviation from desired shape was only studied by the method according to invention. The results of this investigation are given in Table 2. TABLE 2 PARTICLE ANALYSIS There is also for granulated product, good accordance bet¬ ween the two methods of analysis as far as particle size distribution is concerned. Analysis of the deviation of the particles from the desired shape gave, for this type of product too, good accordance with the real conditions. When the particle feed system was connected to a prilling process such that samples were taken from the flow of pro¬ duct, it took all in all less than 5 minutes from change of operation conditions in the relevant part of the process till it was recorded on the particle analyzer. Compared to conventional methods of analysis this is more than fast enough for most particulating processes. It is however possible to reduce the total time of analysis, and hence the response time too, without this influencing the quality of the analysis and the accuracy. Tests have shown that the automatic particle analyzer is well suited for particles in the measurement range 0,5- 10,0 mm, but with small physical changes it is fully possible to displace this measurement range considerably. Furthermore it has shown that dust in the particle samples gives no problems. A special application which was carried out on order, was analysis of particles with different colours/shades of grey. During testing it appeared that one for example, could de¬ termine the number of black and light particles in a sample. This was achieved by applying a contrast plate during photo¬ graphing the particle curtain. At the same time, analysis of particle size distribution could be carried out. Through the present invention one has achieved a particle feeding means which in a consistent and practical form can transfer a particle sample to a particle curtain in the form of a monolayer of particles that is representative for the particle distribution in the sample/product stream. By means of this arrangement representative samples of one or several product streams can quickly be taken and transferred to a monolayer that can be analyzed, particularly with respect to particle size distribution and deviation from desired shape. When analyzing the particles one found it particularly ad¬ vantageous to light these by means of a flash that is auto¬ matically triggered as soon as a picture has been completely treated. For each flash, a photograph of the particles is then taken. This gave a very accurate and quick analysis of the particle curtain. The method and the apparatus according to the invention may be applied to all known particulating processes and pro¬ cesses where addition of particles with the desired size distribution and shape is important. But the invention will be applicable for verification of finished particulated product too. Such applications may be: analysis during bulk loading, packing in bags or similar, or verification of specifications of particulate product. The particle analyzer according to the invention may also be applied when analyz¬ ing small samples in laboratories.

Claims: AMENDED CLAIMS [received by the International Bureau on 9 May 1989 (09.05.89) original claims 1-7 replaced by new claims 1-4 (2 pages)] 1. Method for automatic analysis for determining the size distribution of particles and their deviation from desired shape and colour, including collec¬ tion of particle samples and generation of a par¬ ticle curtain in monolayer form, lighting of said monolayer and recording of pictures that are ana¬ lyzed, and being presented at at least one place, c h a r a c t e r i z e d i n t h a t particles in monolayer form are generated by tak¬ ing particle samples through a silo whose distance (a) to a below positioned vibrating plate has a length relative to the distance (b) between the outer edge of the plate and the centre line of the silo, which is large enough for the particles that are flowing out of the silo and down onto the plate and out over its edge when it vibrates, forms an angle et with the horizontal plane, and that the angle o is 95 - 50 % of the sliding angle of the particulate material. 2. Method according to claim 1, c h a r a c t e r i z e d i n t h a t when analyzing particles of different colour or shades of grey, a contrast device with the shade of grey/colour to be excluded in the picture camera is applied. 3. Means for execution of the method according to claims 1-2 and including sampler means (1) , c h a r a c t e r i z e d i n t h a t said means in addition to the sampler (1) com¬ prises a silo (3) with at least one level sensor (4) for recording the level of particles in the silo (3) and for giving signal to the sampler (1) for collection of samples, and a vertical dis- placeable extension (6) at the outlet opening of the silo (3) and where the lower part of the ex¬ tension (6) is at a distance (a) from a plate (8) having adjustable vibration. 4. Means according to claim 3, where the plate (8) is circular, c h a r a c t e r i z e d i n t h a t the plate (8) has a conicity smaller than the angle of.

Inventors: ASBJOERNSEN ODD ANDREAS, JOERGENSEN TERJE, STRAND ODDBJOERN ERIK, ASBJOERNSEN, ODD, ANDREAS, JOERGENSEN, TERJE, STRAND, ODDBJOERN, ERIK
Applicants: NORSK HYDRO AS, NORSK HYDRO A.S
Application year: 1988
Main classification: G01N15
IPC codes: G01N15, G01N25