METHOD FOR ANALYZING IMPURITIES IN LIQUID AND APPARATUS THEREFOR

Abstract: A method for analyzing impurities in liquid and an appara­ tus therefor are disclosed, which are adapted to classify impu­ rities contained in various liquids to be measured into soluble substance, insoluble substance and impurities in the form of bubbles and to measure their concentration separately; espe­ cially the impurities in liquid are analized by the method such that photoacoustic signals obtained by irradiating a liquid to be measured with intensity-modulated light are measured; the correlation between the modulation frequency of the intensity-­ modulated light (light modulation frequency) and the phase of the intensity-modulated light, with which the liquid to be mea­ sured is irradiated, as well as that of their photoacoustic sig­ nals are obtained; and impurities in the liquid to be measured are detected, while classifying them into soluble and insoluble ones and those in the form of bubbles on the basis of the infor­ mation thus obtained: and the apparatus comprises a light source (3), at least one light modulator (5, M₁, M₂, M₃) for transforming light from the light source (3) into intensity-modu­ lated light having a given constant frequency, at least one cell (2, 2a, 2b, 2c) disposed at a position, where it is irradiated with the intensity-modulated light, and containing liquid to be mea­ sured, at least one phase detection device (1, 1a, 1b, 1c) for detecting the phase of the photoacoustic signals coming from the cell (2, 2a, 2b, 2c), a calculating device (7) for analyzing im­ purities in the liquid on the basis of this phase detection device (1, 1a, 1b, 1c), and a control device (4) for controlling the mod­ ulation frequency (light modulation frequency) of the intensity-­ modulated loght in the light modulator (5, M₁, M₂, M₃).

Description: BACKGROUND OF THE INVENTION This invention relates to a method and an apparatus for analyzing impurities in liquid in accordance with claims 1 and 6, respectively. A method and an apparatus of this kind are known from Patent Abstracts of Japan, Vol. 8, No. 269 (page 319) [1706], 8 Dec. 1984 and JP-A-59 136 638. It is known that the photoacoustic spectroscopy is useful for a highly sensitive spectroscopic analyzing method, when it is applied to liquid samples and used as a colorimetric analyzing apparatus. Shohei Oda, Tsuguo Sawada and Hitoshi Kamada have reported in an article entitled "Determination of Ultra Trace Cadmium by Laser-Induced Photoacoustic Absorption Spectrometry", Analytical Chemistry, Vol. 52, p. 650 (1980), that cadmium can be analyzed down to 12 ppt in the form of a complex salt with dithizone by means of a photoacoustic analyzing apparatus. Further, Shohei Oda, Tsuguo Sawada, Toyohiko Moriguchi and Hitoshi Kamada have reported that when the photoacoustic analyzing method is applied to suspension of barium sulfate its detection limit is 30 ppb in an article entitled "Analysis of Turbid Solution by Laser-Induced Photoacoustic Spectroscopy", Analytical Chemistry, Vol. 52, p. 650 (1980). It has been shown in this example that the calibration curve of the suspension doesn't depend on the diameter of particles, when light modulation frequency is set at 33 Hz. That is, it has been clarified that the photo-acoustic analyzing method has a characteristic that it is not influenced by the diameter of suspended particles. However, on the other hand, it has been verified by Kitamori, et al. that the phase of photo-acoustic signal relative to that of the light modulation frequency (in the following abbreviated as "the phase of the photo-acoustic signal") depends on the diameter of suspended particles and and that the diameter and the concentration of suspended particles can be measured by the photoacoustic analyzing method. In this way, it has been verified that the photoacoustic analyzing method can be applied to highly sensitive analyzing and is useful not only for analysis of true solutions but also for that of suspensions. However, no technique has been known, which is adapted to measure separately not only insoluble impurities but also soluble ones (impurities in the form of ions) in liquid, utilizing such characteristics as described above of the photoacoustic analyzing method. This is because theoretical relations between measurement conditions such as the light modulation frequency for the photoacoustic analyzing apparatus and information obtained under those conditions are not known. Furthermore, the amount of impurities contained in ultra-pure water is in the order of ppt's and this concentration level is below the lower detection limit of the conventional analyzing method such as chromatography, colorimetry, etc. Consequently, it is difficult to apply the prior art analyzing methods to analysis of impurities in ultra-pure water. The above mentioned prior art document, Patent Abstracts of Japan, Vol. 8, No. 269, (page 319) [1706], 8 Dec. 1984 and JP-A-59 136 638 discloses a measuring method for the grain size distribution. Photo-acoustic signals obtained by irradiating impurities in a liquid sample with intensity-modulated light which is able to excite the impurities are measured as follows: The phase of the photo-acoustic signal is taken as a measure of the diameter of the impurities; the intensity of the photo-acoustic signal is proportional to the concentration of the impurities; and the signal to noise ratio of the intensity of the photo-acoustic signal improves when the intensity-modulated frequency is equal to the oscillation frequency of the piezoelectric element or cell used as phase-detector. Therefore, the grain size distribution can be measured while the intensity-modulated frequency is equal to the oscillation frequency or near thereof. However, the mentioned prior art document deals only with measuring insoluble impurity concentration profiles (particles suspended in a liquid). As stated above, none of the conventional impurity analyzing methods achieves the classification of impurities which are contained in a liquid into insoluble substance, soluble substance, and further impurities in the form of bubbles. SUMMARY OF THE INVENTION The object of this invention is to provide a method for analyzing impurities in liquid and an apparatus therefor, which are adapted to classify impurities in liquid to be measured into at least soluble and insoluble impurities. As a refinement the method and the apparatus should be able to further classify impurities in the form of bubbles, and to measure their concentration separately. The above object is solved by the features set out in claim 1 (method) and 6 (apparatus), respectively. The dependent claims 2 to 5 characterize advantageous developments of the method according to claim 1, while the dependent claims 7 to 21 each characterize an advantageous development of the apparatus according to claim 6. In the following, explanation will be made of the construction of the apparatus for classifying the kinds of impurities in liquid into soluble and insoluble ones and, according to a preferred embodiment, also in the form of bubbles by referring to Fig. 1 and Table 1. Explanation of notation ρ s : specific weight of particles C Ps : specific heat of particles h : heat transfer coefficient from particles to medium d c : lower detection limit of radius of particles  Q : phase delay due to propagation of photoacoustic signals  D : phase delay due to delay in time necessary for heat evacuation after incidence of light to particles S : intensity of photoacoustic signals The principle of this invention is based on the fact that the relation between the light modulation frequency and the phase of the photoacoustic signals varies depending on the property of impurities, as indicated in Table 1. Hereinbelow, the principle on the basis of which the relation between the measurement conditions and information, as indicated in Table 1, can be obtained will be explained, according to the theory of the inventors of this invention on generation, propagation and detection of photoacoustic signals. Impurities absorbing periodically intensity-modulated light produce periodically heat by nonradiative processes. This heat induces periodical thermal expansion of the medium and as the result generates acoustic waves. The generated acoustic waves, i.e. photoacoustic signals are represented by P ( , t), where represents a vector in an arbitrarily set spatial coordinate system and t represents time. The photoacoustic signals can be described as acoustic waves by the following wave equation; where C is the sound velocity, β is the thermal expansion coefficient of the medium, C P is the specific heat of the medium, H ( , t) represents the time and spatial distribution of heat generated by the nonradiative processes, and is a differential operator with respect to the vector . The solution of this wave is in general given by the following equation; where F is a Fourier transformation operator; ( ', ω), etc. are Fourier images of a function H( , t); and G( | ') is a Green function determined by the boundary conditions given by the structure, materials, etc. of the cell. The concrete representation of the photoacoustic signals P( , t) is given by the structure and the materials of the cell as well as the concrete representation of the function H( , t). In the case where the impurities are soluble, since the solution is a true solution, the spatial distribution of H( , t) coincides with the spatial distribution of the projected light. Further, in the case where the nonradiative relaxation time of the impurities is sufficiently short and negligeable with respect to the period of the light modulation, the time distribution of H( , t) coincides with the time distribution of the projected light. Consequently, the following equation can be obtained; where α is an absorption coefficient of the solution; I₀ is the intensity of the projected light; R( ) represents the spatial distribution of the projected light; and M(t) represents the time distribution of the projected light and is called the modulation function. Using Eqs. (2) and (3), P₁( , t) representing the photoacoustic signals for soluble impurities is given by a representation (4) as follows; Next, in the case where the impurities are insoluble, a representation for the photoacoustic signals can be deduced as follows. As indicated in Fig. 2, an impurity particle 41 absorbs light 42 and releases heat produced by a radiationless transition in the form of a thermal flux 43 in the medium. Representing this thermal flux by J, J is given by the following equation, which is produced according to a temperature field T(ρ, t) formed around the impurity particle; where ρ indicates a vector representing the position of the impurity particle in the coordinate system; λ is the heat conduction coefficient of the medium; and indicates the normal vector. The temperature field T(ρ, t) can be obtained by using the following heat equations; where K is the heat diffusion coefficient; indicates the region inside of the impurity particle; and the characters with suffix S indicate that the properties represented by the respective characters are concerned with the impurity particle. In the case where impurity particles are distributed uniformly in the cell, H( , t) can be obtained by using the following equation; where N is the density in number of the impurity particles and it is related to the impurity concentration C by the following equation; where σ indicates the density and V represents the volume of the impurity particles. ∫ S in Eq. (8) indicates integration over the surfaces of the impurity particles. In the case where the impurity particles are sufficiently small and the temperature of all the impurity particles varies uniformly, by resolving Eqs. (5) to (9), ( , ω) is represented by Eq. (10) as follows; Substituting ( , ω) of Eq. (10) for Eq. (2), the photoacoustic signals P₂( , t) coming from the impurity particles can be obtained by using the following equation; where When the modulation function M(t) is a sinusoidal function having an angular frequency ω₀, since Eqs. (4) and (11) can be transformed into the following equations; where Q(r, t) = iω₀∫ r' R(r')G(r|r')dr' (16). When the diameter of impurity particles is nearly zero, Eq. (15) coincides with Eq. (14) and the photoacoustic signals from a liquid containing insoluble impurities become identical to those from a true solution. In order to make the intensity and the phase of the photoacoustic signals more distinctive, Eqs. (14) and (15) may be represented in a polar coordinate system, as follows; where Q = |Q(r, t)| (19) Consequently,  Q represents the phase delay due to propagation of the photoacoustic signals and  D indicates the phase delay of the photoacoustic signal due to the time interval required for release of heat produced in the impurity particles. By using Eqs. (12) to (22), the conditions for the classification of the impurities and the measurement of their concentrations, as indicated in Table 1, can be obtained. At first, in the case where the light modulation angular frequency ω₀ sufficiently satisfies σ S C Ps ω₀ << S V h (23), and the following equation is valid; it can be seen from Eq. (18) that the intensity of the photoacoustic signal is independent of the size of the impurity particles. Furthermore, in this case, from Eq. (22)  D = 0 can be obtained. Thus, only  Q gives the phase delay of the photoacoustic signal in Eqs. (17) and (18) so that the phase of the photoacoustic signal from the liquid containing insoluble impurities coincides with that from a solution containing soluble impurities. Since the photoacoustic signal is an acoustic wave having linear characteristics, the principle of superposition is applied to the signal. Under these conditions, the intensity of the photoacoustic signal corresponds to the sum of the concentration of soluble impurities and that of insoluble ones and the resultant phase is  Q . Therefore, when the phase ϑ of the lock-in amplifier for the photoacoustic signal is set at ϑ =  Q , the intensity of the phase-detected photoacoustic signal represents the total amount of impurities contained in the solution. On the other hand, when ω₀ satisfies and  D is distinguishable from  Q , it can be understood that the insoluble impurities can be measured separately from soluble ones. In this case, the size of the impurity particles can be known from Eq. (22) and thus, in the case where the impurities particles can be assumed to be spherical, since S = 4πd² and V = 4 / 3πd³ in Eq. (22), the radius d of the impurity particles is given by In addition, for the conditions given by Eqs. (23) and (24) the following relationship is valid; S V h = 3h d (26). This means that, in the case where  D = 0, even if the projected light is modulated with a light modulation frequency satisfying Eq. (24), the impurities are not particles but all of them are soluble. In the case where the impurities are in the form of bubbles, the projected light is refracted by bubbles, changes its path and can enter directly the detector. In this case, the incident light produces photoacoustic signals of the detector itself. However, since the light velocity is much greater than the sound velocity, the phase of the photoacoustic signal is zero. Consequently, it is possible to measure bubbles, distinguishing them from soluble and insoluble impurities. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a block diagram showing the basic structure of this invention; Fig. 2 is a schematic diagram for explaining the process of absorbing light and releasing heat; Fig. 3 is a block diagram showing the first embodiment of this invention; Fig. 4 is a system diagram showing the second embodiment of this invention; Fig. 5 shows graphs indicating measurement examples obtained by using the apparatus indicated in Fig. 4; Fig. 6 is a system diagram showing the third embodiment of this invention; Fig. 7 is a system diagram showing the fourth embodiment of this invention; and Fig. 8 shows graphs indicating measurement examples obtained by using the apparatus indicated in Fig. 7. DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinbelow the embodiments of this invention will be explained, referring to the drawings. Fig. 1 is a block diagram showing the basic structure of this invention. Light emitted by a light source enters a light modulator 5, in which the incident light is transformed into intensity-modulated light, whose intensity varies with a constant frequency, and a cell 2 containing a liquid sample to be measured is irradiated with this intensity-modulated light. The reference numeral 1 represents a phase detection device having functions to receive photoacoustic signals obtained at the cell 2 and measure the phase and the intensity of the photoacoustic signal or to take out only the photoacoustic signal which has a given phase from the received signal and measure its intensity. The reference numeral 4 indicates a control device, which sets the light modulation frequency in the light modulator 5 and also the phase in the phase detection device 1. The reference numeral 7 represents a calculating device, which classifies impurities contained in the liquid sample, calculates their amount (concentration), and displays results, if necessary, on the basis of information obtained by the phase detection device 1. Fig. 3 shows the first embodiment of an apparatus for analyzing impurities in liquid, in which the light modulation frequency can be set at any desired value and a lock-in amplifier is used as the phase detection device 1 for detecting the phase of the photoacoustic signals, the phase and the sensitivity of the lock-in amplifier 1 also being settable at any desired values. The light modulation frequency as well as the phase and the sensitivity of the lock-in amplifier are controlled by the control device coupled with a calculator on the basis of Table 1. In this embodiment a sample such as ultra-pure water, etc. is prepared and filled in a sealed type cell 2 and the photoacoustic signal derived from the sample is measured. In this apparatus an Ar laser device is used as the light source 3 and a light beam of 2.6 W having an oscillation line of 488 nm is utilized as exciting light. In this apparatus, the light modulation frequency is set at 80 Hz for low frequency modulation and at 410 kHz for high frequency modulation. These light modulation frequencies sufficiently satisfy Eqs. (23) and (24), respectively, for particles of silicon dioxide having a radius of 1 µm in water. Once the low frequency modulation is selected, the phase of the lock-in amplifier 1 is set automatically at a value as mentioned before by the controller (control device) 4 and measures only the intensity of the photoacoustic signal. In this way, the total amount of impurities (concentration) in the sample can be obtained. In this case, the lower detection limit of the light-absorption coefficient is about 10⁻⁸/cm. Further, when the impurities are silicon dioxide particles, they can be measured down to about 20 ppt. When the measurement of the total amount of impurities is terminated, the light modulation frequency is set automatically at the high frequency side and the lock-in amplifier acts as a phase detector. In this case, for a particle radius of 1 µm the phase is 45 degrees and the smallest measurable value of the phase detector of 0.5 degree corresponds to a particle radius of about 0.1 µm. In addition, in the embodiment shown in Fig. 3, the reference numeral 5 is the photoacoustic modulator transforming light coming from the Ar laser 3 into modulated light; 6 is the oscillator feeding the lock-in amplifier 1 and the photoacoustic modulator 5 with signals; and 7 represents the calculator (calculating device). Further, since a photoacoustic modulator 5 is used as the light modulator 5, an oscillator 6 is disposed, which drives the modulator. Next, the second embodiment of the apparatus according to this invention will be explained, referring to Fig. 4. In this embodiment, flow type cells are used and 2 sets of light modulators M₁, M₂, cells 2a, 2b combining the same sample and lock-in amplifiers 1a, 1b are disposed. These 2 sets are adjusted for different measurement conditions. The light source 3 is an Ar laser device having an output 20 W. The light modulator M₁ is set at 80 Hz and M₂ at 410 kHz. The setting value of these light modulation frequencies can be varied by the control device 4. The lock-in amplifier 1a measures the intensity S₁ and 1b measures variations in phase  D and the intensity S₂. The measured values S₁, S₂ and  D are processed by a calculator 7. Further, in the figure, the reference numeral 8 indicates a light distributing device disposed between the light source 3 and the light modulators M₁, M₂, that is, 8a is a beam splitter, which directs the incident light beam toward 2 directions, and 8b is a mirror, which reflects the incident beam. The liquid sample 35 flows successively through the cells 2a and 2b by means of a pump 36. Fig. 5 shows an example of measurements according to this embodiment. The figure shows that soluble impurities of 20 ppb flows in the region A and impurities of 60 ppt having a particle radius of 0.3 µm are detected in the region B. In the region C impurities of 30 ppt in the form of particles having a particle radius of 0.15 µm are detected. In the region D no impurities are detected. The relationship between the intensity of signals and the concentration in this apparatus is as follows; Soluble impurity concentration = signal intensity (µV) x 2 (ppb/µV) (27) Insoluble impurity concentration = signal intensity (µV) x 2 (ppt/µV) (28) In this case, for the soluble impurities, calculations were effected, assuming that the molecular light absorption coefficient is 10 (mol. cm⁻²). Furthermore, it can be seen that at E and F bubbles are detected. Fig. 6 shows the third embodiment of this invention, in which the method according to this invention is applied to an ultra-pure water production apparatus. In the figure, the reference numeral 10 indicates a raw water supply line for feeding a distillation tower 11 with raw water such as city water; 12 is an activated charcoal filter tower for eliminating organic impurities; 13 is an inverse osmotic membrane module for eliminating particles, electrolyte, etc.; 14 is an intermediate tank; 15 is an ion exchange resine tower for eliminating electrolyte, etc.; 16 is a pure water tank for storing produced pure water (specific resistance greater than 1 - 10 MΩcm); 17 is an ultra-violet ray sterilizer for sterilizing bacteria; 18 is a polisher for eliminating electrolyte; and 19 is an ultra-filtration membrane module for eliminating fine particles. This ultra-filtration membrane module 19 feeds a 5-way valve 20 with ultra-pure water, whose specific resistance is greater than 17-18 MΩcm and in which the number of fine particles larger than 0.1-0.2 µm is smaller than 50/cc and that of living bacteria is smaller than 0.1/cc. Further, in the figure, 21 to 24 represent water sending pumps or pressuring pumps. Produced ultra-pure water is supplied successively from the 5-way valve 20 to the cells 2a, 2b and 2c of the apparatus 25 for analyzing impurities. 3a indicates a light source utilizing a high energy CO₂ laser; 9a is a beam splitter; 9c is a half mirror; 9b is a mirror; M₁, M₂ and M₃ are light modulators; 1a, 1b and 1c are lock-in amplifiers; 4 is a controlling device controlling the light modulators M₁ to M₃ and the lock-in amplifiers 1a to 1c; and 7 is a calculating device for classifying impurities into various sorts and calculating their concentration on the basis of information coming from the lock-in amplifiers 1a to 1b. This calculating device 7 is provided also with the function to control a valve 10a mounted on the raw water supply line 10, the 5-way valve 20 and another valve 27, depending on analysis results of the produced ultra-pure water. The light modulation frequency ω₁ of the light modulator M₁ is set at 33 Hz and the light frequencies ω₂ and ω₃ of the light modulators M₂ and M₃, respectively, are set at 4 MHz. The phase of the lock-in amplifiers 1a and 1b is set at  D = 48° obtained previously experimentally. The total amount of impurities and the amount of soluble impurities are measured on the basis of the intensity of the photoacoustic signals S₁ and S₂, respectively. The lock-in amplifier 1c measures the phase  and the intensity S₃ of the photoacoustic signals. Thus, the mean radius of particles of insoluble impurities is obtained from the phase  and the concentration of the insoluble impurities is calculated on the basis of the intensity S₃. The signals coming from the lock-in amplifiers 1a-1c are directly inputted to the calculating device 26 and control the 5-way valve 20 described above as follows. If S₁ > 100 µV → Stop of water supply (the valve 10a is closed.) If S₂ > 50 µV → Redoing of purification after the inverse osmotic membrane module 13 or the ion exchange resine tower 15. If S₃ > 50 µV and at the same time  > 0.5° → Redoing of purification by returning water to the upstream of the pure water tank 16 or the ultra-filtration membrane module. For the above described conditions it is assumed that purification is repeated, if the amount of soluble impurities is greater than about 1 ppb and if the amount of insoluble impurities is greater than 10 ppt and at the same time their particle radius is greater than 0.3 µm. Further, when the phase of the lock-in amplifier 1c is 0, since bubbles are mixed in the ultra-pure water, the valve 27 is commuted to the side of a degassing device 28 and after having degassed the ultra-pure water, it is supplied to a use point for example for semi-conductor production. Furthermore, although all the produced ultra-pure water passes through the apparatus for analyzing impurities 25 in this embodiment, in the case where the capacity of the pure water production apparatus is large, the analyzing apparatus 25 can be also so constructed that only a part of the produced ultra-pure water is bypassed therethrough. Fig. 7 shows the fourth embodiment of this invention, in which an apparatus for analyzing impurities according to this invention is applied to industrial waste water. In the figure, the reference numerals, which are used also in Fig. 4 or Fig. 6, represent identical or corresponding parts. The reference numeral 29 indicates a waste water ejecting line; 30 is a waste water treatment installation; 31 is a storing reservoir; and 32 is a sampling device. Samples taken in this sampling device 32 are supplied successively to the cells 2a, 2b and 2c of the apparatus for analyzing impurities. In this embodiment an Ar laser device of 5 W is used as the light source 3. The other conditions are identical to those described for the embodiment illustrated in Fig. 6. The photoacoustic signals (PA signals) coming from the cells 2a to 2c are inputted to the lock-in amplifiers 1a to 1c, respectively, and the intensities S₁ to S₃ of the photoacoustic signals from the lock-in amplifiers 1a to 1c as well as the phase  D of the photoacoustic signals from the lock-in amplifier 1c are inputted to the display-recording device (calculating device) 7. The samples, which have passed through the cells 2a to 2c, are ejected by the drain. Fig. 8 shows a result obtained by analyzing industrial waste water by means of the apparatus indicated in Fig. 7. As indicated above, the apparatus for analyzing impurities according to this invention can be applied to the case where samples to be analyzed are turbid and suspended. According to the embodiments described above of this invention the following effects can be obtained. 1) It is possible to classify impurities into soluble and insoluble ones as well as bubbles in liquid and to measure their concentration separately. 2) It is possible to analyze an extremely small amount of impurities (order of ppt), because the photoacoustic spectroscopic method is applied to the detection. 3) It is possible to analyze also turbid samples, because the photoacoustic spectroscopic method is utilized for the detector. 4) It is possible to monitor impurities in liquid, because on-line measurement can be effected. Consequently, when this method is applied to the water quality control of ultra-pure water, on-line control of the water quality can be effected and production yield in semiconductor process and genetic engineering plant is increased. As explained above, according to this invention, since impurities in liquid are analyzed on the basis of information on the modulation frequency of intensity-modulated light, with which liquid samples are irradiated, the relationship between the phase of the intensity-modulated light and that of the photoacoustic signal, and the intensity of the photoacoustic signal, it is possible to classify impurities in liquid into soluble and insoluble ones and those in the form of bubbles and also to measure their concentration separately.

Claims: A method for analyzing impurities in a liquid, comprising the steps of measuring at least the phase of photo-acoustic signals obtained by irradiating a liquid to be measured with intensity-modulated light being able to excite said impurities, setting the light modulation frequency to a predetermined constant frequency which depends on the specific weight of the particles, the specific heat of the particles, the heat transfer coefficient from the particles to the liquid medium and the lower detection limit of the radius of the particles, obtaining the relationship between the modulation frequency of said intensity-modulated light and the received phase of information of said photo-acoustic signals relative to the phase of said light modulation frequency; and detecting and classifying said impurities in the liquid to be measured into at least soluble and insoluble ones on the basis of said relationship. The method according to claim 1, wherein said kinds of the impurities to be classified further comprise bubbles. The method according to claim 1 or 2, in which, when the phase ⊖ of the photo-acoustic signals with respect to the phase of the intensity-modulated light, with which the liquid to be measured is irradiated, satisfies; ϑ = 0 , it is judged that bubbles are mixed therein; when ϑ =  Q , where  Q indicates the phase delay due to the propagation of the photoacoustic signals, it is judged that soluble impurities are mixed therein; and further when ϑ =  Q +  D , where  D is the phase delay due to the time which elapses from irradiation of the particle with light to release of heat, it is judged that insoluble impurities are mixed therein. The method according to one of the preceding claims, wherein the concentration of impurities which are classified into soluble and insoluble ones as well as those in the form of bubbles is obtained on the basis of the intensity of the photo-acoustic signals. The method according to claim 3 or 4, in which, when the phase ⊖ of the photoacoustic signals is represented by ϑ =  Q +  D , the mean particle radius of the insoluble impurities is calculated on the basis of the value of  D . An apparatus for analyzing impurities in liquid comprising: a light source (3); at least one light modulator (5, M₁, M₂, M₃) transforming light from said light source (3) into intensity-modulated light having a selected constant modulation frequency; at least one cell (2, 2a, 2b, 2c) disposed at a position, where it is irradiated with said intensity-modulated light and containing liquid to be measured; at least one phase detection device (1, 1a, 1b, 1c) for detecting the phase of the photo-acoustic signals coming from the cell (2, 2a, 2b, 2c); a calculating device (7) receiving information from the phase detection device (1, 1a, 1b, 1c) and analyzing the relationship between the modulation frequency of the intensity-modulated light and the received phase information of the photo-acoustic signals relative to the phase of said light modulation frequency, and thereby classifying the impurities in the liquid to be measured into at least soluble and insoluble ones; and a control device (4) for controlling the modulation frequency of the intensity-modulated light in said modulator (5, M₁, M₂, M₃) to a predetermined frequency which depends on the specific weight of the particles, the specific heat of the particles in the liquid, the heat transfer coefficient of the particles to the liquid medium and the lower detection limit of the radius of the particles. The apparatus according to claim 6, in which said phase detection device (1, 1a, 1b, 1c) has a function to detect photo-acoustic signals having a predetermined phase among those received by it, and a control device is disposed for setting said predetermined phase. The apparatus according to claim 6 or 7, in which only one control device (4) controls said light modulator (5, M₁, M₂, M₃) as well as said phase detection device (1, 1a, 1b, 1c). The apparatus according to claim 6 or 7, in which said phase detection device (1, 1a, 1b, 1c) has a function to amplify the photo-acoustic signals thus obtained and the control device (4) of said phase detection device (1, 1a, 1b,1c) controls its phase as well as its sensitivity. The apparatus according to one of the claims 6 to 9, in which, when insoluble impurities are detected in the liquid to be measured, said calculating device (7) calculates the particle radius of impurities on the basis of the phase of the photo-acoustic signals thus detected. The apparatus according to claim 6, in which, for measuring the total amount of the impurities said control device (4) controls said light modulator (5, M₁, M₂, M₃) and said phase detection device (1, 1a, 1b, 1c) so that the light modulation frequency ω of said light modulator (5, M₁, M₂, M₃) satisfies; where ρS is the specific weight of particles to be measured; C Ps is the specific heat of the particles; dc is the lower detection limit of the radius of the particles; and h represents the heat transfer coefficient from the particles to the medium; and at the same time the phase ϑ of the phase detection device (1, 1a, 1b, 1c) for detecting the phase of the photoacoustic signals satisfies; ϑ =  Q , where  Q indicates the phase delay due to the propagation of the photoacoustic signals. The apparatus according to one of the claims 6 to 10, in which for classifying impurities in the liquid into soluble and insoluble ones as well as those in the form of bubbles, said control device (4) controls said light modulator (5, M₁, M₂, M₃) so that the light modulation frequency ω of said light modulator (5, M₁, M₂, M₃) satisfies; where ρS is the specific weight of particles to be measured; C Ps is the specific heat of the particles; dc is the lower detection limit of the radius of the particles; and h represents the heat transfer coefficient from the particles to the medium. The apparatus according to one of the claims 6 to 12, in which a display device is disposed for displaying at least the classified kind of the impurities. The apparatus according to one of the claims 6 to 13, in which said phase detection device (1, 1a, 1b, 1c) is a lock-in amplifier. The apparatus according to claim 14, in which said light modulator (5, M₁, M₂, M₃) is a photoacoustic modulator and an oscillator (6) is disposed between said light modulator (5, M₁, M₂, M₃) and said control device (4) for controlling them, whereby the light modulation frequency of said light modulator (5, M₁, M₂, M₃) is controlled by controlling the oscillation frequency of said oscillator (6) by means of said control device (4) and reference signals coming from said oscillator (6) are applied to said lock-in amplifier. The apparatus according to claim 6, in which a plurality of sets, each of which consists of a light modulator (5, M₁, M₂, M₃), a cell (2a, 2b, 2c), and a phase detection device (1, 1a, 1b, 1c), for analyzing photoacoustic signals are arranged in parallel to each other so that each of a plurality of light beams coming from said light source (3) enters the cell (2a, 2b, 2c) of each of the sets, the light modulation frequencies in different light modulators being so controlled that they are different from each other; at the same time the liquid to be measured flowing through the cells (2a, 2b, 2c) one after another. The apparatus according to claim 16, in which two light modulators (M₁, M₂), two cells (2a, 2b), and two phase detection devices (1a, 1b) are disposed in parallel, respectively, so that the first and the second analyzing sets are constructed; for said first analyzing set the light modulation frequency ω₁ being so controlled that it satisfies; where ρS is the specific weight of particles to be measured; C Ps is the specific heat of the particles; dc is the lower detection limit of the radius of the particles; and h represents the heat transfer coefficient from the particles to the medium; the phase ϑ of the phase detection device (1a, 1b) for detecting the phase of the photoacoustic signals being set so that it satisfies; ϑ =  Q , where  Q indicates the phase delay due to the propagation of the photoacoustic signals; and further for said second analyzing set the light modulation frequency ω₂ is so controlled that it satisfies; The apparatus according to claim 16 or 17, in which there exists only one light source (3) and a light distributing device (8, 9a, 9b, 9c) is disposed between said light source (3) and each of said light modulators (M₁, M₂, M₃) so that light emitted by said light source (3) is splitted into a plurality of light beams, each of which enters each of said light modulators (M₁, M₂, M₃). The apparatus according to claim 18, in which said light distributing device (8) consists of a beam splitter (8a) and a mirror (8b). The apparatus according to claim 16, in which the number of analyzing sets is greater than two and said light distributing device consists of a beam splitter (9a), at least one half mirror (9c), and a mirror (9b). The apparatus according to claim 16, in which three light modulators (M₁, M₂, M₃), three cells (2a, 2b, 2c) and three phase detection devices (1a, 1b, 1c) are disposed in parallel, respectively, so that the first, the second and third analyzing sets are constructed; for said first analyzing set the light modulation frequency ω₁ being so controlled that it satisfies; where ρS is the specific weight of particles to be measured; C Ps is the specific heat of the particles; dc is the lower detection limit of the radius of the particles; and h represents the heat transfer coefficient from the particles to the medium; for said second and third analyzing sets the light modulation frequency ω₂ being so controlled that it satisfies; for the first and second analyzing sets the phase ϑ of the phase detection device (1a, 1b) for detecting the phase of the photoacoustic signals being set so that it satisfies; ϑ =  Q , where  Q indicates the phase delay due to the propagation of the photoacoustic signals; whereby the concentration of the whole impurities is calculated on the basis of the intensity (S₁) of the photoacoustic signals coming from the phase detection device (1a) of said first analyzing set; the concentration of the soluble impurities is calculated on the basis of the intensity (S₂) of the photoacoustic signals coming from the phase detection device (2a) of said second analyzing set; and the concentration and the particle radius of the insoluble impurities are calculated or bubbles are detected on the basis of the intensity (S₃) and the phase ϑ of the photoacoustic signals coming from the phase detection device (3a) of said third analyzing set.

Inventors: KAWASAKI, SATORU, KITAMORI, TAKEHIKO, KONDO, MASAHIRO, UCHIDA, SHUNSUKE
Applicants: HITACHI, LTD.
Application year: 1985
Main classification: G01N21
IPC codes: G01N21, G01N29