METHOD OF DETECTING CHARACTERISTICS OF RESIN IN INJECTION MOLDING MACHINE

Abstract: A method of detecting the characteristics of resin in an injection molding machine having an on-off operating mechanism for the flow path of the resin and a method of controlling the weight of the injected resin on the basis of the detected characteristics of the injected resin. Such an arrangement is adopted that, in a state where the aforesaid flow path on-off operating mechanism is closed after the resin is plasticized and measured, processes, in which urging forces of predetermined urging values po, p are applied to the screw to balancingly move the screw until it stops, are successively carried out under a given molten state value Z of the resin, and the relationship between the urging value po, p and the moving distance Sr of the screw are approximated by a given functional equation, to thereby obtain the relationship between a molten resin pressure P and a molten resin volume.

Description: FIELD OF THE INVENTION The present invention relates to a method for detecting the resin property of plasticized synthetic resin in an injection moulder which has a flow path opening/closing mechanism in the passage between the cylinder of the moulder and the cavity of a mould so as to block the resin flow between the cylinder and the cavity, and to an injection control method for controlling the weight of the plasticized synthetic resin injected from the cylinder of the injection moulder to fill the cavity of the form, on the basis of the detected resin property. BACKGROUND OF THE INVENTION In a coventional injection moulding of plasticized synthetic resin by an injection moulder, the weight of the injected plasticized synthetic resin varies with the pressure of molten resin, the specific volume of the molten resin or the molten state of the resin indicated by the temperature of the molten resin etc. (including the influence of the disturbance on the moulding system). Therefore, it is difficult to form products of a constant quality. To cope with this problem, a number of proposals, so-called adaptive control, have been made The art disclosed in JP-A- 81 084 932 is an example. Basically, in the adaptive control method, when the influence of a disturbance on the moulding system and a change in the molten resin pressure, molten resin temperature or mould temperature are detected, a controllable moulding condition (pressure, time, etc.) other than the detected factors is changed into a control factor, thereby assuring a constant product quality. However, this control method has the following disadvantages: 1. Preliminary study and analysis are necessary to determine the correlation between the detected factor according to the mould and the product quality and between the control factor and the product quality. 2. With the same plasticized synthetic resin, the correlation between the detected factor and the product quality and between the control factor and the product quality varies greatly depending on the mould. Therefore, the study and analysis described in the item 1 above must be repeated each time the mould is changed. In injection moulding processes are generally described with respect to the plasticized synthetic resin property such as the PVT property, P denoting the pressure of molten resin v, the specific volume of the molten resin and T, the temperature of the molten resin (= molten state)]. Based on this fact, some proposals have been made to control the moulding process by use of the PVT property, such as described on pages 11 and 12 of Modern Plastics International, Oct. 1989. This PVT property-based control method also has the following problems: (i) To control the moulding process by use of the PVT property, the PVT property must be given or determined in advance for practical use. Determination of the PVT property requires accurate measurement using a special measurement instrument in a test facility. (ii) Various kinds of plasticized synthetic resins are used in actual injection moulding and, in many cases, new plasticized synthetic resins are introduced one after another. Therefore, if the PVT property of a certain type of plasticized synthetic resin is to be obtained experimentally, to provide the experimental determination of the PVT property of all the plasticized synthetic resins to be used would involve enormous time and expense and is not feasible. (iii) Moreover, for the same plasticized synthetic resin, the experimentally determined PVT property does not always coincide with the PVT property in an injection moulder actually used at the injection moulding site for the following reason. In an experimental equipment, the plasticized synthetic resin is heated only externally. In an actual injection moulder, in contrast, the thermal history and extremely large shearing force during the melting process of the plasticized synthetic resin cause a slight change in the molecular distribution of the resin. Consequently, the melting behaviour of the resin in the actual injection moulder may be different from that in the experimental equipment. (iv) Furthermore, for recycled use of waste resin material, the actual injection moulding may use reclaimed plasticized synthetic resin by mixing new plasticized synthetic resin material. Even if new plasticized synthetic resin pellets are used, the quality of the pellets may vary among different production batches or even in the same production batch. Accordingly, it is very difficult to apply the experimentally obtained PVT property directly to the actual injection moulding. The molten resin temperature (T) as the PVT property, or the molten state such as flowability of resin indicated by the molten resin temperature (T) can also be indicated by the revolution or back-pressure of the screw, the time required for measuring the molten resin in the actual injection moulding, or a combination of some of these three factors. Therefore, the PVT property can be generalized by replacing the molten resin temperature (T) with the molten state (Z). It is an object of the present invention to solve the above problems in the resin property-based moulding process control method. Specifically, an object of the present invention is: (i) to provide a method for detecting the resin property of plasticized synthetic resin, which is capable of: 1 detecting easily the resin property of the plasticized synthetic resin presently used in injection moulders at the actual injection moulding site, and 2 utilizing the thus detected resin property directly for controlling the injection moulding process under way in the site, and (ii) to provide an injection control method capable of calculating an appropriate screw travel distance on the basis of the resin property detected by the above-mentioned detection method by using a given calculation formula, thereby controlling the weight of plasticized synthetic resin injected from the cylinder of the injection molder to fill the cavity of a mould. The article "Qualitaet im Griff mit pmT -Optimierung Fuer Nachdruckphase" by Michaeli and Lauterbach, in "Plastverarbeiter" Vol. 40, No. 10 at pages 43 to 50, October 1989, discloses an injection moulding process in which a production phase is preceded by a learning phase. In the learning phase, the weight of the moulded articles are weighed to enable pmT characteristic curves to be developed, in denoting the weight of the moulded articles. The result of the learning phase are evaluated in that the quality characteristics of the moulded articles produced in the learning phase and those articles which achieve the quality desired in production are identified by the operator in the controller. The production phase is controlled by controlling the dwell pressure and time to maintain a combination of parameters to result in moulded articles which should have the desired quality characteristics. According to one aspect of the present invention, a resin property detection method for an injection moulder which has a flow path opening/closing mechanism between the cylinder of the injection moulder and the cavity of a mould so as to block the flow of the plasticized synthetic resin between the cylinder and the cavity wherein a screw of the injection moulder is rotated with the opening/closing mechanism closed to cause the screw to move back, is characterised in that the following two process stages are conducted sequentially, with plasticized synthetic resin of a specified molten resin state value Z in front of the screw: (a) a first process stage comprising the steps, in the closed state of the flow path opening/closing mechanism to block the flow of plasticized synthetic resin, applying a reference pushing force value P₀ to the screw to effect a balancing movement of the screw under the blocked state of flow and obtaining the positional value of the screw at the reference stop position where the screw stops its balancing movement, and (b) a second process stage comprising the steps of applying a pushing force value P, different from the reference pushing force P₀, to the screw to effect a balancing movement of the screw, obtaining the positional value of the screw at the position where the screw stops its balancing movement, and calculating the travel distance S T from the reference stops position of the screw; and in that a relational formula for the molten resin pressure value P and the molten resin volume value with the specified molten resin state value Z is obtained through the approximation of the relation among the pushing force values P₀ and P and the travel distance S T by using the functional equation:- f(P/P₀) = exp{a.( P/P₀ - 1} in which P₀ is the reference molten resin pressure value (reference pushing force value P₀), P is the molten resin pressure value (pushing force value p) a is a constant. According to another aspect of the present invention, a resin property detection method for an injection moulder which has a flow path opening/closing mechanism between the cylinder of the injection moulder and the cavity of a mould so as to block the flow of plasticized synthetic resin between the cylinder and the cavity, wherein a screw of the injection moulder is rotated with the resin flow blocked to cause the screw to move back is characterised in that the following two process stagers are conducted sequentially, with plasticized synthetic resin of a specified molten resin state value Z in front do the screw Z: (a) a first process stage comprising the steps, in the closed state of the flow path opening/closing mechanism to block the flow of plasticized synthetic resin, applying a reference pushing force value P₀ to the screw to effect a balancing movement of the screw under the blocked state of the flow, and obtaining the positional value of the screw at the reference stop position where the screw stops its balancing movement, and (b) a second process stage comprising the steps of applying a pushing force value p, different from the reference pushing force P₀, to the screw to effect a balancing movement of the screw, obtaining the positional value of the screw at the position where the screw stops its balancing movement, and calculating the travel distance S T from the reference stop position of the screw; and said first and second process stages are repeated under different molten state values Z, the pushing force value p to be applied to the screw being varied in the second process stage, and in that the relational formula for the molten resin pressure value p, the molten resin volume value and the molten state value Z is obtained through the approximation of the relation among the pushing force values p₀ and p, the travel distance S T and the molten state value Z by using the functional equation:- f(P/P₀) = exp{a (Z).(√ P/P₀ - 1)} in which P₀ is the reference molten resin pressure value (reference pushing force value p₀), P is the molten resin pressure value (pushing force value p) a(Z) is a constant fixed by the molten resin state value Z. The resin property detection method of the present invention may include the steps of repeating the above first and second process stages under different molten state values Z and under different pushing force values p in the second process stage, and obtaining the relational formula for the molten resin pressure value P, the molten resin volume value and the molten state value Z through the approximation of the relation among the pushing force values p₀ and p, the travel distance S T and the molten state value Z by using a specified functional equation. The molten resin specific volume value V can be obtained by proportional calculation from the molten resin volume value and molten resin specific volume value V calculated in the following procedure: First, the following three process stages are conducted sequentially with the above-mentioned molten state value Z of plasticized synthetic resin: (a) a first process stage comprising the steps of the closing the flow path opening/closing mechanism to block the plasticized synthetic resin flow, and under the blocked state of the flow, applying either of the pushing force values p₀ and p to the screw so as to effect a balancing movement of the screw, and obtaining the positional value of the screw at the first stop position where the screw stops its balancing movement. (b) a second process stage comprising the steps of opening the flow path opening/closing mechanism to allow the plasticized synthetic resin to flow, and under the available state of the flow, applying a pushing force to the screw so as to permit the resin of an appropriate weight value G to be injected. (c) a third process stage comprising the steps of closing the flow path opening/closing mechanism to block the plasticized synthetic resin flow after injecting the plasticized synthetic resin of the weight value G, and under the blocked state of the flow, applying the same pushing force value as that for the first process stage to the screw so as to effect a balancing movement of the screw, and obtaining the positional value of the screw at the second stop position where the screw stops its balancing movement. Then, the molten resin volume of the injected plasticized synthetic resin is obtained on the basis of the positional values of the screw at the first and second stop positions, and finally the molten resin specific volume value V is calculated from the obtained molten resin volume value and the weight value G. Here, if it is necessary to obtain a true molten resin specific volume value V, or in other words, if the type of injection moulder and the moulding condition are to be changed substantially, the above-mentioned proportional calculation to obtain the molten resin specific volume value V, the molten resin volume remaining in front of the screw in the cylinder have to be taken into consideration. If the flow path opening/closing mechanism is a stop valve provided in the nozzle of the injection moulder, the true molten resin specific volume value V can be obtained by calculating the molten resin volume value by the following procedure: i) When the value of the residuel volume of molten resin remaining between the screw end and the stop valve is given as a design value: The given molten resin residual volume value is converted to the travel distance of the screw and added to the aforementioned travel distance S T , and the molten resin volume value of the injected plasticized synthetic resin is calculated from the sum of the travel distances. ii) When the molten resin residual volume value remaining between the screw end and the stop valve is unknown: With plasticized synthetic resin of the molten state value Z, the specified pushing force value p is applied to the screw at different positions, with the stop valve closed to prevent resin flow. As the screw changes its position by a balancing movement under the pushing force value p, the travel distance of the screw from the previous position to the present position is calculated. Extrapolation is used to obtain, from the stop positions and the respective travel distances, the positional value of the screw where the travel distance by the specified pushing force value p becomes zero. This positional value is then added to the aforementioned travel distance S T . The molten resin volume value of the injected plasticized synthetic resin is obtained from the sum of the travel distances. Thus, according to a further aspect of the present invention, a resin property detection method for an injection moulder which has a screw in a cylinder of the injection moulder and a flow path opening/closing mechanism between the cylinder moulder and the cavity of a mould so as to block the flow of plasticized synthetic resin between the cylinder and the cavity is characterised in that the following three process stage are conducted sequentially with plasticized synthetic resin of various molten state values Z: (a) a first process stage comprising the steps of the closing the flow path opening/closing mechanism to block the plasticized synthetic resin flow, and, under the blocked state of the flow applying various pushing force values p to the screw so as to effect a balancing movement of the screw, and obtaining the positional value of the screw at the first stop position where the screw stops its balancing movement under each of said various pushing force values p, (b) a second process stage comprising the steps of opening the flow path opening/closing mechanism to allow the plasticized synthetic resin to flow, and under the available state of the flow, applying a pushing force to the screw so as to permit plasticized synthetic resin of an appropriate weight value G to be injected, and (c) a third process stage comprising the steps of closing the flow path opening/closing mechanism after injecting the plasticized synthetic resin of weight value G to block the plasticized synthetic resin flow, and under the blocked state of the flow, applying said various pushing force values p to the screw so as to effect a balancing movement of the screw, and obtaining the positional value of the screw at the second stop position where the screw stops its balancing movement under each of said various pushing force values p; in that the molten resin volume value of the injected plasticized synthetic resin is obtained on the basis of the positional values of the screw at the first and second stop positions under each of the various pushing force values p for each molten state value Z; and in that the molten resin specific volume value V is calculated from each of the thus calculated molten resin volume values and said weight value G, thereby obtaining the PVZ property relational formula for the molten resin pressure value P, the molten resin specific volume value V and the molten state value Z. Thus, according to the detecting method of the resin property for the injection moulder of the present invention, the resin property of the plasticized synthetic resin presently used for injection moulding can be detected easily in the injection moulder installed at the injection moulding site. Moreover, the thus detected resin property can be utilized directly in controlling the actual injection moulding process at the site. The molten state value Z may be any value selected from among the molten resin temperature, the revolution or back-pressure of the screw, the time required for measuring resin, or a combination of some of these elements. BRIEF DESCRIPTION OF THE DRAWINGS Figs. 1 to 7 are drawings for explaining preferred embodiments of the resin property detection method and the injection control method for an injection moulder according to the present invention; Figs. 1(A) is a semi-diagrammatic vertical sectional view of an injection moulder for forming a product by injection moulding; Fig. 1(B) is an enlarged vertical sectional detail view of the injection moulder; Figs. 2 and 3 are vertical sectional views showing the operation of the screw in first and second embodiments, respectively, of the method of the present invention; Fig. 4 is a graph explaining an extrapolation method for obtaining the molten resin volume value of the residual resin remaining in front of the screw; Fig. 5 is a vertical sectional view showing the operation of the screw for reference in obtaining the calculation formula for the travel distance of the screw for injecting resin of a constant weight value ; and Figs. 6 and 7 are semi-diagrammatical vertical sectional views of moulding systems to which embodiments of a control method are applied. PREFERRED EMBODIMENTS OF THE INVENTION Some embodiments of the resin property detection method for an injection moulder according to the present invention are described with reference to the attached drawings. Referring to the Fig. 1(A), an injection moulder 11 is connected by a nozzle 12 to a mould 10 in which a product is to be formed. A screw 19 is contained in the cylinder 13 of the injection moulder 11. Resin pellets supplied from a hopper 15 are melted and mixed in the cylinder 13, heated by a heater 14, to form a molten plasticized synthetic resin. The amount of molten resin is measured and then injected by the screw 19 through a flow passage 16 formed in the nozzle 12 and through a gate 17 into the cavity 18 of the mould 10. To melt and mix the resin pellets, the screw 19 is rotated by a screw-driving motor 20. The screw 19 and the screw-driving motor 20 are fixed on a base 21 which is moved laterally in the drawing, by means of pressurised oil supplied to a hydraulic piston device 27 through a pipe line 26 from a pressurised oil supply 25. To control the supply o f pressurised oil, an electromagnetic flow valve 22 and an electromagnetic pressure valve 23 are controlled by a controller 24. In other words, the movement of the screw 19 towards and away from the nozzle 12 to measure the amount of molten resin to be injected and to inject the measured ,molten resin into the cavity 18 of the mould 10, and the application of a specified pushing force to the screw 19 to impart a specified pressure to the molten resin in the cylinder 13 are all controlled through the base 21 by the pressurised oil supplied to the hydraulic piston device 27. The base 21 is engaged by a screw position detector 28 for detecting the positional value of the screw 19 in the cylinder 13 the positional value being "0" when the screw is at the left hand end, as seen in the drawing, and increasing as the screw 19 moves towards the right. The screw position detector 28 comprises a potentiometer and an encoder etc. The positional values of the screw 19 detected by the detector 28 minute by minute are sent to the controller 24 as well as to a PVZ arithmetic unit 29 which determines the PVZ property relation formula for plasticized synthetic resin when detecting the resin property P, V and Z referring respectively to the pressure, specific volume and temperature of the molten resin. The PVZ arithmetic unit 29 also operates a PV property relation formula to calculate the travel distance of the screw 19 and supplies the calculated result to the controller 24, thereby controlling the injection. The molten temperature value in the cylinder 13 detected by a resin temperature detector 30 is also transmitted, as the molten state value Z of the molten resin, to the PVZ arithmetic unit 29. The oil pressure value for the hydraulic piston device 27 is detected by an oil pressure detector 31 and is also sent to the arithmetic unit 29 as the pushing force applied to the screw 19 or the molten resin pressure value P in the cylinder 13. The measured volume of injected molten resin is inputted through an input unit 32 to the PVZ arithmetic unit 29 when detecting the resin property. The molten resin pressure value P, molten state value (molten resin temperature value) Z and other conditional values set for detecting the resin property are also input from the external input unit 32 through the PVZ arithmetic unit 29 to the controller 24. The target weight of the molten resin to be injected is also input form the external input unit 32 to the PVZ arithmetic unit 29. The flow passage 16 of the nozzle 12 contains a stop valve 33 as a flow path opening/closing mechanism of the injection moulder for interrupting the flow of molten resin flow. The stop valve 33 is operated through an operating rod 35 by an electromagnetic driving unit 34 which is controlled by the controller 24. As shown in Fig. 1(B) a ring-shaped axially slidable valve plug 39 is provided between the conical end portion 36 and the flange projection 38 at the end of the spiral portion 37 of the screw 19. As the molten resin pressure in front of the screw 19 or at the left hand end of the screw increases, the slidable valve plug 39 is pressed against the flange projection 38, thus preventing the molten resin from flowing back to the right. Thus, the flange projection 38 and the ring-shaped slidable valve plug 39 constitute a check valve 40. Even if the screw position detector 28 reads "0" for the position of the screw 19, residual molten plasticized synthetic resin exists in the space between the front end of the screw 19 and the stop valve 33, or more specifically between the check valve 40 and the stop valve 33. Now, some embodiments of the present invention on the resin property detection method for an injection moulder are described in detail. (First embodiment) For the first phase of the method, the following three process stages are repeated with various molten state values (molten resin temperature values) Z₁, Z₂, Z₃ ...., under a constant value p₀ of the pressure of the molten resin to obtain values V₀₁, V₀₂, V₀₃,... of the specific volume of the molten resin for the respective molten state values Z₁, Z₂, Z₃, ... (see Fig. 2). 1) First Process Stage The screw 19 is rotated to drive the molten plasticized synthetic resin towards the front end of the screw 19. In the first process stage in which the stop valve 33 is closed, the screw 19 is moved back because of the pressure of the molten resin prevailing in front of the screw 19. While the screw 19 is moved back to a preliminarily set initial position, the amount of the molten resin to be injected is measured. When the screw 19 has reached the initial position, the screw rotation is stopped. The arrival of the screw at the initial position is detected by the screw position detector 28 which sends the positional value of the screw 19 at the initial position to the controller 24. On the basis of this positional value, the controller 24 controls the pressurised oil supply to the hydraulic piston device 27 so that a specified pushing force value p₀ is applied to the screw 19. Under the specified pushing force, the screw 19 makes a forward balancing movement, compressing the molten resin in front of the screw 19 with the aid of the function of the check valve 40. Thus, the molten resin pressure in the cylinder 13 increases. The forward movement of the screw 19 is stopped at a first stop position when the applied pushing force balances the pressure of the compressed molten resin. The screw position detector 28 detects the positional value of the screw 19 at the first stop position and outputs the value to the PVZ arithmetic unit 29. When the screw 19 is at the first stop position, the molten resin pressure value P₀ in front of the screw 19 corresponds to the pushing force value p₀ applied to the screw 19. 2) Second Process Stage The stop valve 33 is opened, and the screw 19 is moved for a specified distance by the pushing force applied to the screw 19, so that molten resin is injected by an amount corresponding to the specified distance. The weight value G of the amount of injected molten resin is measured by an external measuring instrument. The measured weight value G is input from the external input unit 32 to the PVZ arithmetic unit 29. 3) Third Process Stage The stop valve 33 is closed again, and in this state, the oil pressure is controlled by the controller 24 in the same manner as in the first process stage so as to apply the specified pushing force value p₀ to the screw 19. Under the effect of this pushing force, the screw 19 makes a forward or backward balancing movement, thus compressing the molten resin in front of the screw 19 correspondingly. The screw 19 stops at a second stop position when the applied pushing force balances the compressed molten resin pressure. The screw position detector 28 detects the positional value of the screw 19 at the second stop position and transmits the value to the PVZ arithmetic unit 29. The PVZ arithmetic unit 29 calculates the difference S T between the positional value of the first stop position and that of the second stop position, or in other words, the volume of the molten resin corresponding to the weight G of the injected molten resin. The calculated molten resin volume is divided by the weight G to obtain a molten resin specific volume value V₀. Thus, in the first phase, the series of process stages is repeated for various molten state values (molten resin temperature values) Z₁, Z₂, Z₃, ... under a constant specified pushing force value p₀ (molten resin pressure value P₀) to obtain the molten resin specific volume values V₀₁, V₀₂, V₀₃, .... For the second phase, the following two process stages are repeated for various molten state values (molten resin temperature values) Z₁, Z₂, Z₃, ... under various molten resin pressure values P₁, P₂, P₃, ..., to obtain the respective molten resin specific volume values V₁₁, V₂₁, V₃₁, ... ; V₁₂, V₂₂, V₃₂, ... ; V₁₃, V₂₃, V₃₃, ... (see Fig. 3). 1) First Process Stage Similarly to the first process stage of the first phase, the screw 19 is rotated with the stop valve 33 closed. The screw 19 moves back and stops at a preliminarily set initial position while the molten resin at the molten state value Z₀ is measured. Then, a specified pushing force value p₀ is applied to the screw 19 to move the screw 19 forward so that the molten resin is compressed. The screw 19 stops its forward movement at a first stop position when the applied pushing force balances the pressure of the compressed molten resin. The positional value of the screw 19 at the first stop position is detected by the screw position detector 28 and sent to the PVZ arithmetic unit 29. Other operations are the same as those in the first process stage of the first phase. 2) Second Process Stage A specified pushing force value p is applied to the screw 19 with the stop valve 33 remaining closed and the molten state value still at Z₀. This time, the applied specified pushing force value p is increased gradually from p₁ to p₂ to p₃ and so on, with the pushing force value p₀ in the first process stage as a reference, thus gradually compressing the molten resin. When each of the pushing force values p₁, p₂, p₃, ... is applied, the screw 19 makes a balancing movement and stops at a second, third, fourth or subsequent stop position, as shown in Fig.3. The positional value of each stop position is detected by the screw position detector 28 and sent to the PVZ arithmetic unit 29. The PVZ arithmetic unit 29 calculates the difference S T of the positional value at the second, third, fourth or subsequent stop position from the positional value at the first stop position to obtain the values of the reduction in the molten resin volume on the basis of the calculated difference. From each of the thus obtained molten resin volume reduction values and the molten resin specific volume values V₀₁ (V₀₂, V₀₃,...) calculated in the first phase, molten resin specific volume values V₁₁, V₂₁, V₃₁,... (V₁₂, V₂₂, V₃₂,...; V₁₃, V₂₃, V₃₃,...) are obtained by proportional calculation. This proportional calculation is based on the fact that, for the compressed molten resin of the same molten state value (molten resin temperature value) Z and of the same weight value G, the molten resin specific volume value V is obtained from the ratios of molten resin volume values in the case wherein the molten resin pressure value p₀ (pushing force value p₀) is changed to P₁, P₂, P₃,... (pushing force value p₁, p₂, p₃,...). Thus, the series of calculation processes is repeated for each of the molten state values (molten resin temperature values) Z₁, Z₂, Z₃,... under each of the pushing force values p₁, p₂, p₃,... applied to the screw 19 (the molten resin pressure values P₁, P₂, P₃,...), thereby obtaining the molten resin specific volume values V₁₁, V₂₁, V₃₁,...; V₁₂, V₂₂, V₃₂,...; V₁₃, V₂₃, V₃₃,.... The molten state value (molten resin temperature value) Z is changed by controlling the heater 14 by means of the controller 24. Even with the screw 19 indicating at a position of the positional value "0", residual molten resin remains between the front end of the screw 19 and the stop valve 33. As various pushing forces are applied to the screw 19, this residual molten resin is compressed. This results in the positional values of the screw 19 at respective stop positions. Accordingly, if the PVZ property relation formula established for a particular injection moulder is applied to another injection moulder whose residual molten resin volume value is different from that in the particular injection moulder, the calculation result will contain a large error that cannot be ignored. In such a case, the residual molten resin volume must be corrected to obtain an accurate molten resin specific volume value V. The correction method is described below: i) When the residual molten resin volume value is known as a design value for the equipment and given in terms of the travel distance S₀ of the screw 19: With the molten resin of the same molten state value (molten resin temperature value) Z and of the same weight value G, pushing force values p X and p Y are applied sequentially to the screw 19 after the molten resin has been measured. When the molten resin pressure value becomes P X or P Y and the screw 19 stops its movement, the positional value S x or S y of the screw 19 at the stop position is detected. The travel distance S₀ is added to each of these positional values S x and S y to obtain each of these corrective positional values S X ( = S x + S₀) and S Y ( = S y + S₀) . Then, the molten resin specific volume values V X and V Y can be expressed by the following equations, respectively. V X = (π/4·D²·S X )/G (1) V Y = (π/4·D²·S Y )/G (2) D : diameter of the screw By taking the ratio of these equations, the following equation holds: V X /V Y = S X /S Y ( = (S₀ + S x )/(S₀ + S y )) (3) If the molten resin specific volume value V Y is the molten resin specific volume values V₀₁, V₀₂, V₀₃, ... obtained in the first phase, the molten resin specific volume value V X can be calculated easily from equation (3). Since the present embodiment of the invention obtains the molten resin specific volume value V similarly by calculating the ratios, the above method can be used directly in the present embodiment. ii) When the residual molten resin volume value is unknown: As shown in Fig. 4, the compression amount of the molten resin or the travel distance S of the screw 19 for the compression is proportional to the molten resin volume before compression or the positional value S m of the screw 19 before compression. The graph of a linear function is drawn by changing the positional value S m of the screw 19 in steps for a constant molten resin pressure value P and a constant molten state value (molten resin temperature value) Z. The travel distance S₀ is obtained easily by extrapolation on this graph. Other operations are the same as those described above. For the third phase, each of the molten resin pressure values P₀, P₁, P₂,..., each of the molten resin specific volume values V₀₁, V₀₂, V₀₃,...; V₁₁, V₁₂, V₁₃,...; V₂₁, V₂₂, V₂₃,... and each of the molten state values (molten resin temperature value) Z₁, Z₂, Z₃,... obtained in the first and second phases are substituted in the general formula for the PVZ property, to establish the PVZ property relation formula. Meanwhile, it is possible to obtain the following generalized function from the equation (3): V/V₀ = f(P/P₀) (4) wherein P, V are the given molten resin pressure value and molten resin specific volume value for the given molten resin pressure value P₀, V₀ are the reference molten resin pressure value and molten resin specific volume value for the reference molten resin pressure value The above molten resin pressure values P and P₀ and molten resin specific volume values V and V₀ are given at the same molten state value (molten resin temperature value) Z. From equation (4), the inventor has found that the PV property can be approximated by the following empirical formula: f(P/P₀) = exp{a(√ P/P₀ - 1)} (5) wherein a is a constant Therefore, if the value for the constant "a" is obtained by changing the given molten resin pressure value P, the PV (Z = constant) property relation formula can be obtained. Further, the inventor has found that the value of the constant "a" is a function of the molten state value (molten resin temperature value) Z and can be approximated as follows: a(Z) = b·Z + c (6) wherein b, c are constants The following general formula can be obtained from equations (4), (5) and (6): V = V₀ · exp{(b·Z + c)·(√ P/P₀ - 1)} (7) When each of the molten resin pressure values P₀, P₁, P₂,..., each of the molten resin specific volume values V₀₁, V₀₂, V₀₃,...; V₁₁, V₁₂, V₁₃,...; V₂₁, V₂₂, V₂₃,... and each of the molten state values (molten resin temperature values) Z₁, Z₂, Z₃,... obtained in the first and second phases are substituted in equation (7), the constants "b" and "c" are fixed so that the PVZ property relation formula can be established. If the molten resin specific volume value V₀ for the reference molten resin pressure value P₀ is obtained with the molten state value (molten resin temperature value) Z varied, the molten state value (molten resin temperature value) Z and the molten resin specific volume value V are approximated as expressed by the following linear equation: V₀ = α · Z + β (8) wherein α, β are constants Therefore, when equation (8) is substituted in equation (7), the following equation results: V = (α·Z + β)·exp{(b·Z + c)·(√ P/P₀ - 1)} In the above calculations, the constant "a" was approximated by a linear equation. When the molten state value (molten resin temperature value) Z changes, the constant "a" changes with the molten state value (molten resin temperature value) Z as a variable. Therefore, the constant "a" can be modified to be adaptable to actual equipment by using the polynomial approximation of the molten state value (molten resin temperature value) Z as indicated by the following equation: a(Z) = b'· Z m + b''· Z m-1 + ... + b m' · Z + c' wherein b', b'' ... b m' , c' are constants Similarly, with a constant molten resin pressure value P, when the molten state value (molten resin temperature value) Z changes, the molten resin specific volume value V₀ changes with the molten state value (molten resin temperature value) Z as a variable. Therefore, it is preferable to employ the following polynomial approximation of the molten state value (molten resin temperature value) Z: V₀ = α'· Z n + α''· Z n-1 + ... + α n' · Z + β' wherein α', α'', ... α n' , β' are constants (Second Embodiment) Now the second embodiment of a resin property detection method according to the present invention is described. For this embodiment, only the process stages different from those in the first embodiment are described, with the description of the same process stages omitted. The PVZ property relation formula is established by repeating the following three process stages for each of the molten state values (molten resin temperature values) Z., Z₂, Z₃,.... 1) First Process Stage Similar to the first process stage of the first phase of the first embodiment, the screw 19 is rotated with the stop valve 33 closed, and stopped when it has moved back to a preliminarily set initial position. Then, pushing force values p S0 , p S1 , p S2 , ..., p Sn are applied sequentially to the screw 19 to compress the molten resin. Under each of these pushing force values p S0 , p S1 , p S2 , ..., p Sn , the screw 19 makes a balancing movement and stops at a first stop position indicated by the positional value S S0 , S S1 , S S2 , ..., or S Sn , which is detected by the screw position detector 28 and sent to the PVZ arithmetic unit 29. Other operations are the same as those in the first process stage of the first phase in the first embodiment. 2) Second Process Stage A pushing force value p, which is applied immediately before injection in the ordinary production process, is applied to the screw 19 and the stop valve 33 is opened, so that the molten resin of the weight for bone batch is injected into the cavity 18 of the mould 10 to form an actual product. Next, a pushing force value p, which is applied during the dwell following the injection in the ordinary production process, is applied to the screw 19 and the stop valve 33 is closed. The weight value G of the injected molten resin is measured by an external measuring instrument and input through the external Input unit 32 to the PVZ arithmetic unit 29. 3) Third Process Stage Similarly to the first process stage, pushing force values p S0 , p S1 , p S2 , ..., p Sn are applied sequentially to the screw 19. Under each of these pushing force values p S0 , p S1 , p S2 , ..., p Sn , the screw 19 makes a balancing movement and stops at a second stop position indicated by the positional value S F0 , S F1 , S F2 , ..., or S Fn , which is detected by the screw position detector 28 and sent to the PVZ arithmetic unit 29. In a series of above-mentioned process stages, the molten resin of the weight value G is injected "n" times. Accordingly, for a constant molten state value (molten resin temperature value) Z, the following equation holds: wherein A is the projected sectional area of the screw 19 S₀ is the travel distance of the screw 19 converted from the residual molten resin volume value The following equation is obtained by substituting equation (4) in equation (5): By using the above equation (10), the formula for such relation between the molten resin pressure (P) and the weight value G of the molten resin injected by one injection operation that will not have an adverse effect on an actual moulded product can be obtained. By substituting equation (10) in equation (9), the following equation holds: Equation (11) is the PV property relation formula for a constant molten state value (molten resin temperature value) Z. The PVZ arithmetic unit 29 operates according to this equation (11) to establish the PV property relation formula for a constant molten state value (molten resin temperature value) Z. A similar process is repeated for each of the molten state values (molten resin temperature values) Z₁, Z₂, Z₃,... to establish the PVZ property relation formula for each molten state value. In the first and second embodiments, the molten resin temperature value is used for the molten state value Z which indicates the molten state of plasticized synthetic resin. The revolution of the screw 19 during plasticization and measurement of the resin, the time required for the measurement, or the back-pressure value of the screw 19 may be used instead of the molten resin temperature value. Even if the revolution or back-pressure value of the screw 19 is constant, the time required for measurement tends to change with the ratio of the reclaimed resin content or of the additive content in the plasticized synthetic resin material etc. The back-pressure value of the screw 19 varies with the temperature of the pressurised oil supplied to the hydraulic piston device 27. This change in the back-pressure value can be identified by detecting the oil pressure for the hydraulic piston device 27 by the oil pressure detector 31. If the revolution or back-pressure value of the screw 19 is to be detected at the time of changing the moulding condition, the revolution or the value of the back-pressure value to be set for the value at the time of new moulding condition may be input through the external input unit 32 to the PVZ arithmetic unit 29. The similar PVZ property relation formula can be established in this case. Therefore, when a continuous moulding operation is started, the travel distance of the screw 19 to the position for injection may be calculated according to the PVZ property relation formula based on the revolution or back-pressure value detected, as a molten state value Z, during the continuous moulding process. In the first and second embodiments, the following equation is used to establish the PVZ property relation formula: V = V₀ · exp{a(Z)·(√ P/P₀ - 1)} Alternatively, Spencer & Gilmore's equation as shown below may be used: wherein T is the molten resin temperature value (molten state value Z) π₁, ω, R' are constants determined by the type of plasticized synthetic resin The values for the constants π₁, ω and R' may be obtained by the following procedure: Firstly, the molten resin specific volume value V₀ under a constant molten resin pressure value P₀ and at a constant molten resin temperature value T₀ is obtained in the same method as in the first phase of the first embodiment. Secondly, under the same molten resin pressure value P₀, the value for the constant ω is obtained with the molten resin temperature value T varied. Then, at the constant molten resin temperature value T₀, the molten resin volume value is obtained with the molten resin pressure value P set at P₁, in the same method as in the second phase of the first embodiment, and the molten resin specific volume value V₁ under the molten resin pressure value P₁ is calculated from the above-mentioned molten resin specific volume value V₀ by proportional calculation. On the basis of the molten resin pressure values P₀ and P₁, the molten resin specific volume values V₀ and V₁ and the constant ω, the value for the constant π₁ can be calculated by the following equation: When the values for the constants ω and π₁ have been obtained, it is possible to calculate the value for the constant R' by equation (12). For other types of plasticized synthetic resin, the values for the constants ω, π₁ and R' may be obtained by the above procedures, if necessary. As mentioned earlier, since the molten resin temperature value T indicates the molten state such as flowability of the molten resin, the molten resin temperature value T can be generalized as the molten state value Z by the following equation: The method of establishing the PVZ property relation formula by using Spencer & Gilmore's equation has been described. Alternatively, the PVZ property relation formula may be established by using the experimental analysis method according to the experimental design (multivariable sequential approximation). Embodiments of an injection control method are based on the PVZ property relation formula thus established by the above procedure. Prior to explaining each embodiment of the injection control method, the calculation formula used to obtain the travel distance of the screw 19 for injecting a constant weight value of molten resin is explained with reference to Fig. 5. First, for plasticized synthetic resin of a constant molten state value Z₁, molten resin pressure value P, positional value S of the screw 19 and molten resin specific volume value V immediately before injection and those during the dwell following the injection are set as follows: The values immediately before injection: Molten resin pressure value : P I1 Positional value of the screw 19 : S I1 Molten resin specific volume value : V (P I1 , Z₁) The values during the dwell following injection: Molten resin pressure value : P H1 Positional value of the screw 19 : S H1 Molten resin specific volume value : V (P H1 , Z₁) The positional values S I1 and S H1 of the screw 19 are based on the distance from the position of the screw 19 indicated by the positional value "0". These positional values S I1 and S H1 are corrected values based on the residual molten resin volume. The weight value G of the molten resin injected by one injection operation into the cavity 18 of the mould 10 can be expressed as follows: in which A is the projected sectional area of the screw 19 This equation (13) can be rewritten as follows: The travel distance S D of the screw 19 to the position for injection is expressed as follows: S D = S I1 - S H1 (15) When equation (15) is substituted in equation (14) and rearranged, the following equation is obtained: In equation (16), the projected sectional area A of the screw 19 is known. The positional value S I1 of the screw 19 immediately before injection is detected by the screw position detector 28. The molten resin specific volume values V(P I1 ,Z₁) and V(P H1 ,Z₁) are obtained from the PVZ property relation formula that has been established in the aforementioned procedure on the basis of the molten resin temperature value (molten state value) Z and molten resin pressure values P I1 and P H1 detected by the resin temperature detector 30 and by the oil pressure detector 31, respectively, or on the basis of the molten state value (molten resin temperature value) Z₁ and molten resin pressure values P I1 and P H1 to be set. Therefore, by using equation (16), it is possible to obtain the travel distance S D of the screw 19, which keeps the injected resin weight value G constant. (Third Embodiment) An embodiment of injection control method is now described on the assumptions that the screw position detector 28 detects the positional value S I1 of the screw 19 immediately before injection, the resin temperature detector 30 detects the molten resin temperature value (molten state value) Z₁, and the oil pressure detector 31 detects the molten resin pressure values P I1 and P H1 immediately before injection and during the dwell following injection, and that each of these detectors outputs the detected value to the PVZ arithmetic unit 29, as shown in Fig. 6. First, the injection weight value G, as the target weight value of a product, is input through the external input unit 32 to the PVZ arithmetic unit 29. The screw 19 is rotated and moves back while the amount of molten resin to be injected is measured. After the rotation of the screw 19 is stopped, a pushing force is applied to the screw 19. Then, the screw position detector 28 detects the positional value S I1 of the screw 19 immediately before injection, with the stop valve 33 closed. At the same time, the oil pressure detector 31 detects the molten resin pressure value P I1 (or pushing force value p I1 ), and the resin temperature detector 30 detects the molten resin temperature value (molten state value) Z₁. These values are input to the PVZ arithmetic unit 29. The stop valve 33 is then opened so that injection is started. As the screw 19 is moved forward, the cavity 18 of the mould 10 is filled with the injected molten resin. When the cavity 18 has been almost completely filled up, the dwell process starts. The molten resin pressure value P H1 (pushing force value p H1 ) during the dwell process following the injection is also detected by the oil pressure detector 31 and input to the PVZ arithmetic unit 29. The PVZ arithmetic unit 29 then calculates the travel distance S D of the screw 19 by equation (16), from the input positional value S I1 , molten resin pressure values P I1 and P H1 and molten resin temperature value (molten state value) Z₁, on the basis of the PVZ property relation formula. The calculated travel distance S D is sent to the controller 24 where it is compared with the positional value provided by the screw position detector 28. When the travel distance S D is equal to the positional value, the controller 24 closes the stop valve 33, thus terminating the injection of the molten resin into the cavity 18 of the mold 10. Thus, according to this embodiment, the travel distance S D for injection of the resin of a constant weight value G can be obtained even if the molten resin pressure values P I1 and P H1 and the molten resin temperature value (molten state value) Z₁ vary. (Fourth Embodiment) Another embodiment of the injection control method is described on the assumption that the positional value S I1 of the screw 19 immediately before injection is detected and transmitted to the PVZ arithmetic unit 29, and that the molten resin pressure values P I1 and P H1 and molten resin temperature values (molten state value) Z₁ preliminarily set in the controller 24 are also transmitted to the PVZ arithmetic unit 29, as shown in Fig. 7. For this embodiment, only the operations different from those in the third embodiment are described, with the description of same operations omitted. The controller 24 controls the electromagnetic flow valve 22 and electromagnetic pressure valve 23 so that set molten resin pressure values P I1 and P H1 are obtained. The controller 24 also controls the heater 14 so that a set molten resin temperature value (molten state value) Z₁ is obtained. The PVZ arithmetic unit 29 calculates the travel distance S D from the positional value S I1 of the screw 19 immediately before injection input from the screw position detector 28 and the molten resin pressure values P I1 and P H1 and molten resin temperature value (molten state value) Z₁ set in the controller 24, on the basis of the PVZ property relation formula. The calculated travel distance S D is sent to the controller 24. Other operations are the same as those in the third embodiment. In the third embodiment, the latest molten resin pressures values P I1 and P H1 and molten resin temperature values (molten state value) Z₁ detected are used for calculating the travel distance S D . Alternatively, the calculation may be based on the values of P I1 , P H1 and Z₁ detected in the last injection operation or on the mean values of P I1 , P H1 and Z₁ detected in the previous operations over a specified period. The molten resin temperature value is used as the molten state value Z in the third and fourth embodiments. Nevertheless, the revolution of the screw 19 during the plasticization and measurement process, the time required for the measurement or the back-pressure value of the screw 19 may be used for the molten state value Z. As a modified embodiment, instead of the stop valve 33 in the flow passage 16 of the nozzle 12, a shut-off valve may be provided at the gate 17 of the mould 10. POTENTIAL INDUSTRIAL APPLICATION The resin property is easily detected in an injection moulder installed at the injection moulding site by using the plasticized synthetic resin currently used for injection moulding. In addition, the resin property thus detected can be used directly for controlling the actual injection moulding process at the site. Therefore, the resin property detection method for an injection moulder according to the present invention is useful particularly where the property of the plasticized synthetic resin material varies with the ratio of reclaimed resin content or additive content.

Claims: A resin property detection method for an injection moulder which has a flow path opening/closing mechanism (33) between the cylinder (13) of the injection moulder (11) and the cavity (18) of a mould so as to block the flow of the plasticized synthetic resin between the cylinder (13) and the cavity (18), wherein a screw (19) of the injection moulder (11) is rotated with the opening/closing mechanism (33) closed to cause the screw (19)to move back, is characterised in that the following two process stages are conducted sequentially, with plasticized synthetic resin of a specified molten resin state value Z in front of the screw: (a) a first process stage comprising the steps, in the closed state of the flow path opening/closing mechanism (33) to block the flow of plasticized synthetic resin, applying a reference pushing force value P₀ to the screw (19) to effect a balancing movement of the screw under the blocked state of flow and obtaining the positional value of the screw (19) at the reference stop position where the screw stop its balancing movement, and (b) a second process stage comprising the steps of applying a pushing force value P, difference from the reference pushing force P₀, to the screw (19) to effect a balancing movement of the screw, obtaining the positional value of the screw (19) at the position where the screw stops its balancing movement, and calculating the travel distance S T from the reference stop position of the screw; and in that a relational formula for the molten resin pressure value P and the molten resin volume value with the specified molten resin state value Z is obtained through the approximation of the relation among the pushing force values P₀ and P and the travel distance S T by using the functional equation:- f(P/P₀) = exp{a.(√ P/P₀ - 1} in which P₀ is the reference molten resin pressure value (reference pushing force value P₀), P is the molten resin pressure value (pushing force value p) a is a constant. A resin property detection method for an injection moulder which has a flow path opening/closing mechanism (33) between the cylinder (13) of the injection moulder (11) and the cavity (18) of a mould so as to block the flow of plasticized synthetic resin between the cylinder (13) and the cavity (11), wherein a screw (19) of the injection moulder (11) is rotated with the resin flow blocked to cause the screw (19) to move back is characterised in that the following two process stagers are conducted sequentially, with plasticized synthetic resin of a specified molten resin state value Z in front do the screw Z: (a) a first process stage comprising the steps, in the closed state of the flow path opening/closing mechanism (13) to block the flow of plasticized synthetic resin, applying a reference pushing force value P₀ to the screw (19) to effect a balancing movement of the screw under the blocked state of the flow, and obtaining the positional value of the screw (19) at the reference stop position where the screw stops its balancing movement, and (b) a second process stage comprising the steps of applying a pushing force value p, different from the reference pushing force p₀, to the screw (19) to effect a balancing movement of the screw, obtaining the positional value of the screw (19) at the position where the screw stops its balancing movement, and calculating the travel distance S T from the reference stop position of the screw; and said first and second process stages are repeated under different molten state values Z, the pushing force value p to be applied to the screw (19) being varied in the second process stage, and in that the relationship formula for the molten resin pressure value P, the molten resin volume value and the molten state value Z is obtained through the approximation of the relation among the pushing force values p₀ and p, the travel distance S T and the molten state value Z by using the functional equation:- f(P/P₀) = exp{a (Z).(√ P/P₀ - 1)} in which ₀ is the reference molten resin pressure value (reference pushing force value p₀), P is the molten resin pressure value (pushing force value p) a(Z) is a constant fixed by the molten resin state value Z. A resin property detection method for an injection moulder according to claim 1 or 2, further comprising the steps of: conducting the following three process stages sequentially with the plasticized synthetic resin of said molten state value Z: (a) a first process stage wherein the pushing force value P₀ or p is applied to the screw (19) with the flow path opening/closing mechanism (33) closed to block the plasticized synthetic resin flow, so as to effect a balancing movement of the screw, and the positional value for the screw (19) at the first stop position where the screw stops its balancing movement is obtained, (b) a second process stage wherein the flow path opening/closing mechanism (33) is opened to allow the plasticized synthetic resin to flow, and under the available state of the flow, a pushing force is applied to the screw (19) so as to permit plasticized synthetic resin of an appropriate weight value G to be injected, and (c) a third process stage wherein the flow path opening/closing mechanism (33) is closed after injection of the plasticized synthetic resin of weight value G to block the flow of plasticized synthetic resin, a pushing force of the same value as that for the first process stage is applied to the screw (19) in the blocked state of flow so as to effect a balancing movement of the screw, and the position value of the screw at the second stop position where the screw stops its balancing movement is obtained; calculating the molten resin value of injected plasticized synthetic resin on the basis of the positional values of the screw (19) at the first and second stop positions; and obtaining the molten resin specific volume value V from the thus calculated molten resin volume value and the weight value G. A resin property detection method for an injection moulder according to claim 1 or 2, wherein said flow path opening/closing mechanism (33) is a stop valve provided in the nozzle (12) of the injection moulder (11) and the value of the residual volume of the molten plasticized synthetic resin remaining in the space between the from end of the screw (19) and the stop valve (33) is known as a design value, and wherein the residual molten resin volume value is converted into the travel distance of the screw (19) and added to said travel distance S T the injected molten plasticized synthetic resin volume value being obtained from the sum of the travel distances. A resin property detection method for an injection moulder according to claim 1 or 2, wherein said flow path opening/closing mechanism (33) is a stop valve provided in the nozzle (12) of the injection moulder (11) and the value of the residual volume of molten plasticized synthetic resin remaining in the space between the front end of the screw (19) and the stop valve (33) is unknown, and wherein the method further comprises the steps of: applying a specified pushing force value p to the screw (19) at various positions under the blocked state of flow, with the stop valve (33) closed and with plasticized synthetic resin of said molten state value Z; calculating the travel distance of the screw (19) from the last stop position to the position where the screw stops following the balancing movement under said specified pushing force value p; obtaining the positional value of the screw (19) at which the travel distance of the screw becomes zero under said pushing force value p, by the extrapolation on the basis of each stop position and the corresponding travel distance; adding the obtained positional value to said travel distance S T ; and obtaining the molten resin volume value of injected plasticized synthetic resin from the travel distance thus obtained by addition. A resin property detection method for an injection moulder which has a screw (19) in a cylinder (13) of the injection moulder (11) and a flow path opening/closing mechanism (33) between the cylinder (13) and the cavity (18) of a mould so as to block the flow of plasticized synthetic resin between the cylinder (13) and the cavity (18), characterised in that the following three process stages are conducted sequentially with plasticized synthetic resin of various molten state values Z: (a) a first process stage comprising the steps of closing the flow path opening/closing mechanism (33) to block the plasticized synthetic resin flow, and under the blocked state of the flow path applying various pushing force values p to the screw (19) so as to effect a balancing movement of the screw, and obtaining the positional value of the screw at the first stop position where the screw stops its balancing movement under each of said various pushing force values p, (b) a second process stage comprising the steps of opening the flow path opening/closing mechanism (33) to allow the plasticized synthetic resin to flow, and under the available state of the flow, applying a pushing force to the screw (19) so as to permit plasticized synthetic resin of an appropriate weight value G to be injected, and (c) a third process stage comprising the steps of closing the flow path opening/closing mechanism (33) after injecting the plasticized synthetic resin of weight value G to block the plasticized synthetic resin flow, and under the blocked state of the flow, applying said various pushing force values p to the screw (19) so as to effect a balancing movement of the screw, and obtaining the positional value of the screw at the second stop position where the screw stops its balancing movement under each of said various pushing force values p; in that the molten resin volume value of the injected plasticized synthetic resin is obtained on the basis of the positional values of the screw (19) at the first and second stop positions under each of the various pushing force values p for each molten state value Z; and in that the molten resin specific volume value V is calculated from each of the thus calculated molten resin volume values and said weight value G, thereby obtaining the PVZ property relational formula for the molten resin pressure value P, the molten resin specific volume value V and the molten state value Z. A resin property detection method for an injection moulder according to claims 1 to 6, wherein said molten state value Z is a value selected from among the molten resin temperature, the revolution or the back-pressure of the screw (19) and the time required for measuring the molten resin. A resin property detection method for an injection moulder according to any of claims 1 to 3 and 6, wherein said flow path opening/closing mechanism (33) is a stop valve provided in the nozzle (12) of the injection moulder. A resin property detection method for an injection moulder according to any of claims 1 to 3 and 6, wherein said flow path opening/closing mechanism is a shut-off valve provided in the mould for formation.

Inventors: YOKOTA AKIRA KOMATSU LTD PLAST, YOKOTA, AKIRA, KOMATSU LTD.,PLASTIC DIVISION
Applicants: KOMATSU MFG CO LTD, KOMATSU LTD.
Application year: 1991
Main classification: B29C45
IPC codes: B29C45