Process for producing acicular goethite particles and acicular magnetic iron oxide particles

Abstract: Acicular goethite particles are produced by (i) reacting an aqueous ferrous salt solution with less than one equivalent of an aqueous alkali hydroxide solution and/or an aqueous alkali carbonate solution based on Fe²⁺ in said aqueous ferrous salt solution; (ii) blowing a molecular oxygen-containing gas into the ferrous salt reaction solution containing colloidal ferrous hydroxide or iron-containing colloidal precipitates thus obtained so as to oxidize said colloidal ferrous hydroxide or iron-containing colloidal precipitates and to produce acicular goethite nucleus particles; (iii) adding to the resultant aqueous ferrous salt reaction solution containing said acicular goethite nucleus particles not less than one equivalent of an aqueous alkali carbonate solution based on Fe²⁺ in said aqueous ferrous salt reaction solution; and (iv) blowing a molecular oxygen-containing gas into the resulting mixed aqueous ferrous salt reaction solution so as to cause said goethite nucleus particles to grow. Acicular magnetic iron oxide particles may be formed by reducing the acicular goethite particles obtained to produce acicular magnetite particles and, if necessary, the acicular magnetite particles obtained may be oxidised to produce acicular maghemite particles. Also if necessary, the acicular magnetite or maghemite particles may be modified with Co or Co and Fe²⁺.

Description: The present invention relates to a process for producing acicular goethite particles and acicular magnetic iron oxide particles which have a uniform particle size distribution, are substantially free of dendrites, and have a large aspect ratio (major axial diameter:minor axial diameter) and an excellent coercive force distribution. With progressing miniatirization and weight-reduction of magnetic recording and reproducing apparatuses in recent years, the necessity for a recording medium having a higher performance such as a magnetic tape and a magnetic disk has been increasing more and more. In other words, a magnetic recording medium is required to have a higher recording density, higher sensitivity and higher output characteristic. The magnetic characteristics of magnetic particles which are demanded in order to satisfy the above-mentioned requirements for the magnetic recording medium, are a high coercive force and an excellent dispersibility. In order to improve the sensitivity and the output of a magnetic recording medium, the magnetic particles must have as high a coercive force as possible. This fact is described in, for example, DEVELOPMENT OF MAGNETIC MATERIALS AND TECHNIQUE OF IMPROVING THE DISPERSION PROPERTY OF MAGNETIC POWDER (1982), published by K.K. Sogo Gijutsu Kaihatsu Center, p. 310: "Since the improvement of magnetic tapes has been directed toward a higher sensitivity and a higher output, it is an important point to enhance the coercive force of acicular γ-Fe 2 O 3 particles, ..." In order to improve the recording density of a magnetic recording medium, the magnetic recording medium must have a high coercive force and a large residual magnetization (Br), as described in the said DEVELOPMENT OF MAGNETIC MATERIALS AND TECHNIQUE OF IMPROVING THE DISPERSION PROPERTY OF MAGNETIC POWDER. p. 312: "The condition for high-density recording in a coating-type tape is that it is possible to keep the high output characteristics with respect to a short-wavelength signal at a low noise level. For this purpose, it is necessary that both the coercive force (Hc) and the residual magnetization (Br) are large, and that the thickness of the coating film is thin". It is therefore necessary that the magnetic particles have a high coercive force and have excellent dispersibility in the vehicle, and orientation property and packing density in the coating film. In order to enhance the output of a magnetic recording medium, it is required to have a small switching field distribution (hereinunder referred to as "S.F.D.") and hence, the magnetic particles are required to have a small width of coercive force distribution. This fact is described in JP-A-63-26821 (1988): "Fig. 1 is a graph showing the relationship between the S.F.D. of the above-described magnetic disk and the recording and reproducing output. ...The relationship between the S.F.D. and the recording and reproducing output is linear, as is clear from Fig. 1. It indicates that the recording and reproducing output is enhanced by using ferromagnetic powder having a small S.F.D. That is, in order to obtain a large output, an S.F.D. of not more than 0.6 is necessary. As well known, the coercive force of magnetic iron oxide particles depends upon the configurational anisotropy, crystalline anisotropy, strain anisotropy, exchange anisotropy, or the interaction thereof. Acicular magnetite particles and acicular maghemite particles which are used as magnetic iron oxide particles at present show a relatively high coercive force by utilizing the anisotropy derived from their shapes, namely, by increasing the aspect ratio (major axial diameter:minor axial diameter). The known acicular magnetic particles are obtained by reducing as a starting material goethite particles or hematite particles obtained by heat-treating the goethite particles at 280 to 450°C in a reducing gas such as hydrogen, to form magnetite particles, or by further oxidizing the thus-obtained magnetite particles at 200 to 400°C in air to form maghemite particles. The known acicular magnetic iron oxide particles modified with Co or Co and Fe are obtained by dispersing acicular magnetite particles or acicular maghemite particles as the precursor particles in an alkaline suspension containing cobalt hydroxide or an alkaline suspension containing cobalt hydroxide and ferrous hydroxide so that 0.1 to 15.0 atomic% of Co based on Fe of the precursor particles is contained therein and heat-treating the resultant dispersion. The residual magnetization (Br) in a magnetic recording medium depends upon the dispersibility of the magnetic particles in the vehicle, and the orientation property and packing density of the magnetic particles in the coated film: In order to improve these properties, the magnetic particles to be dispersed in the vehicle are required to have as large an aspect ratio (major axial diameter:minor axial diameter) as possible, a uniform particle size distribution and no inclusion of dendrites. As described above, magnetic iron oxide particles which have a substantially uniform particle size distribution, which are substantially free of dendrites and which have a large aspect ratio (major axial diameter:minor axial diameter) are now in the strongest demand. In order to obtain magnetic iron oxide particles provided with these properties, it is necessary that as the starting material goethite particles have a substantially uniform particle size, are substantially free of dendrites and have a large aspect ratio (major axial diameter:minor axial diameter). e.g. an aspect ratio of not less than 20. As a method of producing goethite particles which are the starting material, the following methods are conventionally known: (1) a method of producing acicular goethite particles by oxidizing a suspension containing colloidal ferrous hydroxide which is obtained by adding not less than one equivalent of an aqueous alkali hydroxide solution to a ferrous salt solution, at a temperature of not more than 80°C and pH of not less than 11 by blowing an oxygen-containing gas into the suspension (JP-B-39-5610 (1964)); (2) a method of producing spindle-shaped goethite particles by oxidizing a suspension containing FeCO 3 which is obtained by reacting an aqueous ferrous salt solution with an aqueous alkali carbonate solution, by blowing an oxygen-containing gas into the suspension (JP-A-50-80999 (1975)); and (3) a method of producing acicular goethite nucleus particles by oxidizing an aqueous ferrous salt solution containing a colloidal ferrous hydroxide or an iron carbonate which are respectively obtained by adding not more than one equivalent of an aqueous alkali hydroxide solution or an aqueous alkali carbonate solution to an aqueous ferrous salt solution, by blowing an oxygen-containing gas into the suspension, and then growing the goethite nucleus particles by adding to the thus-obtained aqueous ferrous salt solution containing the goethite nucleus particles not less than one equivalent of an aqueous alkali hydroxide solution based on Fe 2+ in the aqueous ferrous salt solution and blowing an oxygen-containing gas into the resultant aqueous ferrous salt solution for oxidization (JP-B-59-48766 (1984), JP-A-59-128293 (1984), JP-A-59-128294 (1984), JP-A-59-128295 (1984) and JP-A-60-21818 (1985)). Although acicular magnetic iron oxide particles which have a uniform particle size distribution, which are substantially free of dendrites, and which have a large aspect ratio (major axial diameter:minor axial diameter) and excellent coercive force distribution are now in the strongest demand, the particles obtained by the method (1) of producing as a starting material goethite particles contain dendrites and cannot be said to have a uniform particle size distribution in spite of the large aspect ratio (major axial diameter:minor axial diameter), particularly, an aspect ratio of not less than 10:1. According to the method (2), although spindle-shaped particles having a uniform particle size distribution and being free of dendrites are produced, the aspect ratio (major axial diameter:minor axial diameter) thereof is not more than about 7:1. That is, the method (2) is defective in that it is difficult to produce particles having a large aspect ratio (major axial diameter:minor axial diameter). This phenomenon tends to be more prominent as the major axial diameter of the particles become smaller. Various attempts have been made to increase the aspect ratio (major axial diameter:minor axial diameter) of spindle-shaped goethite particles, but the actual aspect ratio (major axial diameter:minor axial diameter) obtained has been not more than about 17 to 18:1, which cannot be said satisfactory. The object of the method (3) is to improve the properties such as particle size, aspect ratio (major axial diameter:minor axial diameter) and the presence or absence of dendrites of the acicular goethite particles produced by the method (1) or (2), but goethite particles produced by the method (3) cannot be said to satisfy the demand for various properties have not been obtained yet. Therefore, acicular magnetic iron oxide particles produced from, as the starting material, these goethite particles cannot be said to have a uniform particle size distribution, to be free of dendrites and to have a large aspect ratio (major axial diameter:minor axial diameter). Accordingly, the present invention seeks to provide acicular goethite particles and acicular magnetic iron oxide particles which have a uniform particle size distribution, which are substantially free of dendrites, and which have a large aspect ratio (major axial diameter:minor axial diameter) and excellent coercive force distribution. As a result of studies undertaken by the present inventors, it has been found that by blowing an oxygen-containing gas into a ferrous salt reaction solution containing colloidal ferrous hydroxide or iron-containing colloidal precipitates which is obtained by reacting an aqueous ferrous salt solution with less than one equivalent of an aqueous alkali hydroxide solution and/or an aqueous alkali carbonate solution based on Fe 2+ in the aqueous ferrous salt solution so as to oxidize the colloidal ferrous hydroxide or iron-containing colloidal precipitates and to produce acicular goethite nucleus particles, adding to the resultant aqueous ferrous salt reaction solution containing the acicular goethite nucleus particles not less than one equivalent of an aqueous alkali carbonate solution based on Fe 2+ in the aqueous ferrous salt reaction solution, and blowing an oxygen-containing gas into the mixed aqueous ferrous salt reaction solution so as to grow the goethite nucleus particles, the thus-obtained acicular goethite particles have a uniform particle size distribution, are substantially free of dendrites, and have a large aspect ratio (major axial diameter:minor axial diameter) and excellent coercive force distribution. On the basis of this finding, the present invention has been achieved. The present invention provides a process for producing acicular goethite particles which process comprises: (i) reacting an aqueous ferrous salt solution with less than one equivalent of an aqueous alkali hydroxide solution and/or an aqueous alkali carbonate solution based on Fe 2+ in said aqueous ferrous salt solution; (ii) blowing a molecular oxygen-containing gas into the ferrous salt reaction solution containing colloidal ferrous hydroxide or iron-containing colloidal precipitates thus obtained so as to oxidize said colloidal ferrous hydroxide or iron-containing colloidal precipitates and to produce acicular goethite nucleus particles; (iii) adding to the resultant aqueous ferrous salt reaction solution containing said acicular goethite nucleus particles not less than one equivalent of an aqueous alkali carbonate solution based on Fe 2+ in said aqueous ferrous salt reaction solution; and (iv) blowing a molecular oxygen-containing gas into the resulting mixed aqueous ferrous salt reaction solution so as to cause said goethite nucleus particles to grow. The present invention also provides a process for producing acicular magnetic iron oxide particles which process further comprises: (v) heat-treating in a reducing gas the thus grown acicular goethite particles or acicular hematite particles obtained by heat-treating the thus grown acicular goethite particles at 300 to 700°C, thereby producing acicular magnetite particles; and (vi) if necessary, oxidizing said acicular magnetite particles, thereby producing acicular maghemite particles. The present invention further provides a process for producing acicular magnetic iron oxide particles which process further comprises: (vii) dispersing said acicular magnetite particles or acicular maghemite particles in an alkaline suspension containing cobalt hydroxide or cobalt hydroxide and ferrous hydroxide so that the Co content in said suspension is from 0.1 to 15.0 atomic% based on the Fe in said magnetite or maghemite particles; and (viii) heat-treating the resultant aqueous dispersion, thereby obtaining acicular magnetite particles or maghemite particles modified with Co or Co and Fe 2+ . In the accompanying drawings: Fig. 1 is an electron micrograph (x 30000) of the particle structure of the acicular goethite nucleus particles obtained in Example 1; Fig. 2 is an electron micrograph (x 30000) of the particle structure of the acicular goethite particles obtained in Example 1; Fig. 3 is an electron micrograph (x 30000) of the particle structure of the acicular goethite particles obtained in Comparative Example 1; Fig. 4 is an electron micrograph (x 30000) of the particle structure of the acicular goethite particles obtained in Comparative Example 2; Fig. 5 is an electron micrograph (x 30000) of the particle structure of the goethite particles obtained in Comparative Example 3; Fig. 6 is an electron micrograph (x 30000) of the particle structure of the goethite particles obtained in Comparative Example 5; and Fig. 7 is an electron micrograph (x 30000) of the particle structure of the goethite particles obtained in Comparative Example 6. As an aqueous ferrous salt solution used in the present invention, an aqueous ferrous sulfate solution and an aqueous ferrous chloride solution may be used. As an aqueous alkali hydroxide solution used for the reaction for producing acicular goethite nucleus particles in the present invention, an aqueous sodium hydroxide solution and an aqueous potassium hydroxide solution are usable. As an aqueous alkali carbonate solution, an aqueous sodium carbonate solution, an aqueous potassium carbonate solution and an aqueous ammonium carbonate solution are usable. The amount of aqueous alkali hydroxide solution and/or aqueous alkali carbonate solution used in the present invention is less than one equivalent based on Fe 2+ in the aqueous ferrous salt solution. If it is not less than one equivalent, the goethite particles obtained have non-uniform particle size distribution and include dendrites and granular magnetite particles. The amount of existent acicular goethite nucleus particles in the present invention is 10 to 90 mol% based on the total amount of goethite particles produced. If it is less than 10 mol%, it is difficult to obtain objective acicular goethite particles. If it exceeds 90 mol%, since the ratio of iron carbonate to the acicular goethite nucleus particles is decreased,the reaction becomes non-uniform and, hence, the particle size distribution of the goethite particles obtained becomes non-uniform. As the aqueous alkali carbonate solution used for growing the acicular goethite nucleus particles, the same alkali carbonate as that used for the reaction for producing acicular goethite nucleus particles is usable. The amount of aqueous alkali carbonate solution used is not less than one equivalent based on Fe 2+ in the residual aqueous ferrous salt solution. If it is less than one equivalent, the goethite particles obtained have non-uniform particle size distribution and include dendrites and spherical magnetite particles. In the present invention, oxidization is carried out by blowing an oxygen-containing gas such as air into a liquid under mechanical stirring, if necessary. The reaction temperature for producing goethite nucleus particles, the oxidization temperature and the reaction temperature for growing goethite nucleus particles in the present invention are not higher than 80°C,which is the temperature for generally producing goethite particles, preferably 30 to 60 °C. If the temperature is higher than 80°C, granular magnetite particles are included in the acicular goethite particles. Before the addition of the aqueous alkali carbonate solution, the thus obtained aqueous ferrous salt reaction solution containing the acicular goethite nucleus particles may be subjected to any one of the following steps. (1) The thus-obtained aqueous ferrous salt reaction solution containing the acicular goethite nucleus particles is heat-treated at a temperature of not less than 75°C, preferably 80 to 95 °C for not less than 0.5 hrs, preferably 1 to 2 hrs; and the resultant aqueous ferrous salt reaction solution containing the acicular goethite nucleus particles is cooled to a temperature of less than 60°C, preferably 30 to 55 °C. (2) The thus-obtained aqueous ferrous salt reaction solution containing the acicular goethite nucleus particles is maintained at a temperature of less than 60°C, preferably 40 to 55 °C in a non-oxidizing atmosphere for not less than 1 hr, preferably 2 to 5 hrs. (3) The thus-obtained aqueous ferrous salt reaction solution containing the acicular goethite nucleus particles is heat-treated at a temperature of not less than 75°C, preferably 80 to 95 °C for not less than 0.5 hrs, preferably 1 to 2 hrs; the resultant aqueous ferrous salt reaction solution containing the acicular goethite nucleus particles is cooled to a temperature of less than 60°C, preferably 30 to 55 °C; and the thus-obtained aqueous ferrous salt reaction solution containing the acicular goethite nucleus particles is maintained at a temperature of less than 60°C, preferably 40 to 50 °C in a non-oxidizing atmosphere for not less than 1 hr, preferably 2 to 5hrs. The magnetic iron oxide particles obtained through the above mentioned steps (1), (2) or (3) have the following superior advantages as compared with those obtained by the basic process of the present invention without using the above-mentioned steps. By step (1), the orientation and squareness of the magnetic iron oxide particles obtained are further improved. By step (2), the S.F.D of the magnetic iron oxide particles obtained is further improved. By step (3), the orientation, squareness and S.F.D. of the magnetic iron oxide particles obtained are further improved. The same reaction column may be used for both the reaction for producing goethite nucleus particles and the reaction for growing the goethite nucleus particles. It is also possible to obtain the objective goethite particles by using different reaction columns for these reactions. It is possible in the present invention to add elements, for example, Co, Ni, Zn, A ℓ , Si and P other than Fe, which are conventionally added in the process for producing goethite particles in order to improve various properties of magnetic particles. In this case, the same advantages are produced. The acicular goethite particles are heat-treated at 300 to 700°C so as to obtain acicular hematite particles. The acicular goethite particles or acicular hematite particles are reduced at 280 to 450 °C in a reducing gas such as hydrogen. The oxidization in the present invention is carried out at 200 to 500°C by an ordinary method. Co-modification (Co-coating) of the magnetic iron oxide particles in the present invention is carried out by an ordinary method. For example, the Co-modification is carried out by dispersing the precursor particles in an alkaline suspension containing cobalt hydroxide or cobalt hydroxide and ferrous hydroxide and heat-treating the dispersion at a temperature of 50 to 100 °C, as described in, e.g., JP-B-52-24237 (1977), JP-B-52-24238 (1977), JP-B-52-36751(1977) and JP-B-52-36863 (1977). The cobalt hydroxide used in the present invention is obtained by reacting a water-soluble cobalt salt such as cobalt sulfide and cobalt chloride with an aqueous alkali hydroxide solution such as an aqueous sodium hydroxide solution and an aqueous potassium hydroxide solution. The ferrous hydroxide used in the present invention is obtained by reacting a water-soluble ferrous salt such as ferrous sulfide and ferrous chloride with an aqueous alkali hydroxide solution such as an aqueous sodium hydroxide solution and an aqueous potassium hydroxide solution. If the temperature is lower than 50°C, it is difficult to produce magnetite particles or maghemite particles modified (coated) with Co or Co and Fe 2+ , and even if they are produced, a very long time for the Co-modification is required. Since the modification arises in the form of a cobalt or ferrous hydroxide, the modification is carried out under a non-oxidizing atmosphere in order to suppress oxidization of the cobalt and iron. The non-oxidizing atmosphere is preferably a stream of an inert gas such as N 2 and argon. The amount of water-soluble cobalt salt used for Co-modification in the present invention is 0.1 to 15.0 atomic% calculated as Co based on Fe of the precursor particles. If it is less than 0.1 atomic%, the coercive force of the acicular magnetite or maghemite particles produced is not improved sufficiently. On the other hand, if it is more than 15.0 atomic%, the coercive force distribution of the acicular magnetite or maghemite particles produced is not improved sufficiently. In consideration of the coercive force and the coercive force distribution of the acicular magnetite particles or maghemite particles, the amount of water-soluble cobalt salt added is preferably 2.0 to 13.0 atomic%. Almost the whole amount of water-soluble cobalt salt added is utilized for the modification of the surfaces of the magnetic iron oxide particles. According to the present invention, when 1 ○ an oxygen-containing gas is blown into a ferrous salt reaction solution containing colloidal ferrous hydroxide or iron-containing colloidal precipitates which is obtained by reacting an aqueous ferrous salt solution with less than one equivalent of an aqueous alkali hydroxide solution and/or an aqueous alkali carbonate solution based on Fe 2+ in the aqueous ferrous salt solution so as to oxidize the colloidal ferrous hydroxide or iron-containing colloidal precipitates and to produce acicular goethite nucleus particles; 2 ○ not less than one equivalent of an aqueous alkali carbonate solution based on Fe 2+ in the aqueous ferrous salt reaction solution is then added to the aqueous ferrous salt reaction solution containing the acicular goethite nucleus particles; and 3 ○ an oxygen-containing gas is finally blown into the mixed aqueous ferrous salt reaction solution so as to grow the acicular goethite nucleus particles in the neutral region (pH of 9 to 10 ), it is possible to obtain acicular goethite particles which have a uniform particle size, which are free of dendrites and which have a large aspect ratio (major axial diameter:minor axial diameter), in particular, an aspect ratio of not less than 20:1, and also it is possible to obtain acicular magnetic iron oxide particles from the acicular goethite particles as a starting material, which have a uniform particle size distribution, which are substantially free of dendrites and which have a large aspect ratio (major axial diameter:minor axial diameter). These acicular magnetic iron oxide particles having these properties also have excellent coercive force distribution. In contrast, in the case of using an aqueous alkali hydroxide solution in place of an aqueous alkali carbonate solution for the reaction for growing the goethite nucleus particles, or in the case of using not less than one equivalent of an aqueous alkali hydroxide solution or an aqueous alkali carbonate solution, it is very difficult to obtain the objective acicular goethite particles which have a uniform particle size distribution, which are free of dendrites and which have a large aspect ratio (major axial diameter:minor axial diameter). The thus-obtained acicular goethite particles have a major axial diameter of not less than 0.1 µm, preferably 0.15 to 0.4 µm, an aspect ratio (major axial diameter:minor axial diameter) of not less than 20:1, preferably 22 to 35:1, and a particle size distribution (a geometric standerd deviation (σ g ) of not less than 0.6, preferably 0.7 to 0.9. The thus-obtained acicular magnetite particles have a major axial diameter of not less than 0.1 µm, preferably 0.12 to 0.4 µm, an aspect ratio (major axial diameter:minor axial diameter) of not less than 6.5:1, preferably 6.7 to 9.0:1, and a particle size distribution (geometric standard deviation (σ g )) of not less than 0.6, preferably 0.62 to 0.80. The thus-obtained acicular maghemite particles have a major axial diameter of not less than 0.1 µm, preferably 0.12 to 0.4 µm, an aspect ratio (major axial diameter:minor axial diameter) of not less than 6.5:1, preferably 6.6 to 8.0:1, and a particle size distribution (geometric standard deviation (σ g )) of not less than 0.6, preferably 0.62 to 0.80. The thus-obtained acicular magnetite particles modified with Co or Co and Fe 2+ have a major axial diameter of not less than 0.1 µm, preferably 0.12 to 0.4 µm, an aspect ratio (major axial diameter:minor axial diameter) of not less than 5.5:1, preferably 5.8 to 7.5:1, a particle size distribution (geometric standard deviation (σ g )) of not less than 0.55, preferably 0.59 to 0.75, and contain 0.1 to 15 atomic% of Co based on Fe of the precursor particles and 0 to 20 atomic% of coated Fe 2+ based on Fe of the precursor particles. The thus-obtained acicular maghemite particles modified with Co or Co and Fe 2+ have a major axial diameter of not less than 0.1 µm, preferably 0.11 to 0.4 µm, an aspect ratio (major axial diameter:minor axial diameter) of not less than 5.5:1, preferably 5.6 to 7.5:1, a particle size distribution (geometric standard deviation (σ g )) of not less than 0.55, preferably 0.58 to 0.75, and contain 0.1 to 15.0 atomic% of Co based on Fe of the precursor particles and 0 to 20 atomic% of coated Fe 2+ based on Fe of the precursor particles. According to the process for producing acicular goethite particles, it is possible to obtain acicular goethite particles which have a uniform particle size, which are substantially free of dendrites and which have a large aspect ratio (major axial diameter:minor axial diameter). The magnetic iron oxide particles obtained from the acicular goethite particles as a raw material in accordance with the present invention also have a uniform particle size, are substantially free of dendrites, and have a large aspect ratio (major axial diameter:minor axial diameter) and excellent coercive force distribution, so that they are suitable as magnetic particles for high-density, high-sensitivity and high-output recording. EXAMPLES The present invention will be explained in more detail in the following Examples. The major axial diameter and the aspect ratio (major axial diameter:minor axial diameter) in each of the following Examples and Comparative Examples are expressed by the average values of the values obtained by measuring the electron micrographs. The particle size distribution is expressed by the geometric standard deviation (σ g ). The major axial diameters of 350 particles were measured from electron micrographs (x 120,000) and the actual major axial diameters were calculated from the measured values. A cumulative amount (%) obtained from the number of the particles belonging to each regular interval of the particle diameter was plotted in a logarithmicro-normal probability paper with particle diameter (µm) as abscissa and cumulative amount (%) as ordinate in accordance with a statistical method from the actual particle diameter and the number of the particles. A particle diameter (D 50 ) when the cumulative amount is 50% and a particle diameter (D 84.13 ) when the cumulative amount is 84,13%, were read out of the obtained log-nomal distribution graph. The geometric standard deviation (σ g ) was found by dividing the particle diameter (D 50 ) by the particle diameter (D 84,13 ) [ σ g =D 50 /D 84,13 ]. The magnetic characteristics and the coating film properties of the magnetic iron oxide particles were measured by using a "sample vibrating type magnetometer VSM-3S-15" (produced by Toei Kogyo K.K.) and applying an external magnetic field up to 5 KOe in case of acicular magnetite particles and acicular maghemite particles, or an external magnetic field up to 10 KOe in case of acicular magnetic iron oxide particles modified with Co or Co and Fe 2+ . A sheet-like sample obtained by a method shown in later-described Example 79 was used for measuring the squareness and the S.F.D. of the coating film. The S.F.D. was measured by using a differentiation circuit of the above-described magnetometer to obtain the differentiation curve of the demagnetizing curve of the magnetism hysteresis curve, measuring a half-width value of the curve and dividing the half-width value by the coercive force. 〈Production of Acicular Goethite Particles〉 Examples 1 to 8 Comparative Example 1 to 6 Example 1 12.8 ℓ of an aqueous ferrous sulfide solution containing 1.50 mol/ℓ of Fe 2+ and 30.2 ℓ of 0.44-N aqueous NaOH solution (the content of NaOH corresponds to 0.35 equivalents based on Fe 2+ in the aqueous ferrous sulfide solution) were mixed to produce at 38°C at pH 6.7 an aqueous ferrous sulfide solution containing Fe(OH) 2 . Air was blown into the aqueous ferrous sulfide solution containing Fe(OH) 2 at a rate of 130 ℓ per minute at 40°C for 3.0 hours, thereby producing goethite nucleus particles. A part of the reaction solution was extracted, filtered out, washed with water and dried by an ordinary method. The electron micrograph (x 30000) of the particles obtained is shown in Fig. 1. To the aqueous ferrous sulfide solution containing the goethite nucleus particles (the amount of existent goethite nucleus particles corresponds to 35 mol% based on the amount of goethite particles produced) were added 7.0 ℓ of 5.4-N aqueous Na 2 CO 3 solution (the content of Na 2 CO 3 corresponds to 1.5 equivalents based on Fe 2+ in the residual aqueous ferrous sulfide solution). Air was blown into the resultant solution at a rate of 130 ℓ per minute at 42°C at pH 9.4 for 4 hours, thereby producing goethite particles. The goethite particles produced were filtered out, washed with water and dried by an ordinary method. The goethite particles produced were acicular particles having a uniform particle size distribution (geometric standard deviation (σ g ) of 0.801), including no dendrites and having an average major axial diameter of 0.33 µm and an aspect ratio (major axial diameter:minor axial diameter) of 25:1, as shown in the electron micrograph (x 30000) in Fig. 2. Examples 2 to 8 Goethite particles were produced in the same way as in Example 1 except for varying the kind, Fe 2+ content and amount of aqueous ferrous salt solution used, the kind, concentration and amount of aqueous alkaline solution used, the kind and amount of additional element, and the reaction temperature in the process for producing goethite nucleus particles; and the kind, concentration and amount of aqueous alkaline solution used, the kind and amount of additional element and the reaction temperature in the process for growing the goethite nucleus particles. The main conditions for production and the properties of the goethite particles obtained are shown in Tables 1 and 2. All of the acicular goethite particles obtained in Examples 2 to 8 had a uniform particle size distribution and no inclusion of dendrites. Examples 9 and 10 Goethite particles were produced in the same way as in Example 1 except for inserting the following step before the addition of the aqueous alkali carbonate solution. The thus-obtained aqueous ferrous sulfide solution containing the goethite nucleus particles was heat-treated under the conditions shown in Table 1 and then cooled to 45 °C. Examples 11 to 13 Goethite particles were produced in the same way as in Example 1 except for inserting the following step before the addition of the aqueous alkali carbonate solution. The thus-obtained aqueous ferrous sulfide solution containing the goethite nucleus particles was maintained under the conditions shown in Table 1. Example 14 Goethite particles were produced in the same way as in Example 1 except for inserting the following steps before the addition of the aqueous alkali carbonate solution. The thus-obtained aqueous ferrous sulfide solution containing the goethite nucleus particles was heat-treated at a temperature of 90 °C for 1 hr, cooled to a temperature of 45 °C and maintained at the same temperature for 2 hrs in a stream of N 2 gas. The main conditions for production and properties of the goethite particles obtained in Examples 9 to 14 are shown in Tables 1 and 2. All of the acicular goethite particles obtained in Examples 9 to 14 had a uniform particle size distribution and no inclusion of dendrites. Comparative Example 1 Goethite particles were produced in the same way as in Example 1 except for using 7.0 ℓ of 5.4-N aqueous NaOH solution (the content of NaOH corresponds to 1.5 equivalents based on Fe 2+ in the residual aqueous ferrous sulfide solution) in place of 7.0 ℓ of 5.4-N aqueous Na 2 CO 3 solution. The particle size distribution of the acicular goethite particles obtained was non-uniform as expressed by a geometric standerd deviation (σ g ) of 0.511 and dendrites were included therein, as shown in the electron micrograph (x 30000) in Fig. 3. Comparative Example 2 Goethite particles were produced in the same way as in Example 1 except for using 30.2 ℓ of 0.44-N aqueous Na 2 CO 3 solution (the content of Na 2 CO 3 corresponds to 0.35 equivalent based on Fe 2+ in the aqueous ferrous sulfide solution) in place of 30.2 ℓ of 0.44-N aqueous NaOH solution, and 7.0 ℓ of 5.4-N aqueous NaOH solution (the content of NaOH corresponds to 1.5 equivalents based on Fe 2+ in the residual aqueous ferrous sulfide solution) in place of 7.0 ℓ of 5.4-N aqueous Na 2 CO 3 solution. The particle size distribution of the acicular goethite particles obtained was non-uniform as expressed by a geometric standerd deviation (σ g ) of 0.516 and dendrites were included therein, as shown in the electron micrograph (x 30000) in Fig. 4. Comparative Example 3 7.5 ℓ of an aqueous ferrous sulfide solution containing 1.0 mol/ℓ of Fe 2+ and 24.2 ℓ of 1.3-N aqueous Na 2 CO 3 solution (the content of Na 2 CO 3 corresponds to 2.1 equivalents based on Fe 2+ in the aqueous ferrous sulfide solution) were mixed to produce FeCO 3 at 42°C at pH 9.9. Air was blown into the aqueous solution containing FeCO 3 at a rate of 100 ℓ per minute at 45°C for 5 hours, thereby producing spindle-shaped goethite particles. To the aqueous solution containing the spindle-shaped goethite particles were added 8.3 ℓ of an aqueous ferrous sulfide solution containing 1.8 mol/ℓ of Fe 2+ and 10 ℓ of 13-N aqueous NaOH solution (the content of NaOH corresponds to 4.4 equivalents based on Fe 2+ in the aqueous ferrous sulfide solution added), and the resultant solution was stirred and mixed (the amount of spindle-shaped goethite particles corresponds to 33 mol% of the amount of goethite particles produced). Air was blown into the resultant mixed solution at a rate of 150 ℓ per minute at 50°C for 3 hours. The goethite particles produced were filtered out, washed with water and dried by an ordinary method. The goethite particles produced had a uniform particle size distribution (geometric standerd deviation (σ g ) of 0.841) and included no dendrites, but they had a small aspect ratio (major axial diameter:minor axial diameter) and took a strip shape, as shown in the electron micrograph (x 30000) in Fig. 5. Comparative Example 4 12.8 ℓ of an aqueous ferrous sulfide solution containing 1.3 mol/ℓ of Fe 2+ and 30.2 ℓ of 2.4-N aqueous NaOH solution (the content of NaOH corresponds to 2.2 equivalents based on Fe 2+ in the aqueous ferrous sulfide solution) were mixed to produce Fe(OH) 2 at 40°C at pH 13.2. Air was blown into the aqueous solution containing Fe(OH) 2 at a rate of 130 ℓ per minute at 45°C for 15 hours, thereby producing acicular goethite particles. The goethite particles produced were filtered out and washed with water by an ordinary method. To 27.5 ℓ of the aqueous solution containing 586 g of the acicular goethite particles were added 12.5 ℓ of an aqueous ferrous sulfide solution containing 1.0 mol/ℓ of Fe 2+ and 10 ℓ of 3.8-N aqueous Na 2 CO 3 solution (the content of Na 2 CO 3 corresponds to 1.5 equivalents based on Fe 2+ in the aqueous ferrous sulfide solution added), and the resultant solution was stirred and mixed (the amount of acicular goethite particles corresponds to 35 mol% of the amount of goethite particles produced). Air was blown into the resultant mixed solution at a rate of 130 ℓ per minute at 42°C for 4 hours. The goethite particles produced were filtered out, washed with water and dried by an ordinary method. The particle size distribution of the goethite particles obtained was non-uniform as expressed by a geometric standerd deviation (σ g ) of 0.512, dendrites were included therein and the aspect ratio (major axial diameter:minor axial diameter) was as small as 10:1. Comparative Example 5 10 ℓ of an aqueous ferrous sulfide solution containing 1.5 mol/ℓ of Fe 2+ and 33 ℓ of 1-N aqueous NaOH solution (the content of NaOH corresponds to 2.3 equivalents based on Fe 2+ in the aqueous ferrous sulfide solution) were mixed to produce colloidal Fe(OH) 2 at 38°C at pH 13. Air was blown into the suspension containing the colloidal Fe(OH) 2 at a rate of 13 ℓ per minute at 42°C for 15 hours, thereby producing acicular goethite particles. The goethite particles produced were filtered out, washed with water and dried by an ordinary method. The particle size distribution of the goethite particles obtained was non-uniform as expressed by a geometric standerd deviation (σ g ) of 0.510 and dendrites were included therein, as shown in the electron micrograph (x 30000) in Fig. 6. Comparative Example 6 10 ℓ of an aqueous ferrous sulfide solution containing 1.5 mol/ℓ of Fe 2+ and 33 ℓ of 1.8-N aqueous solution Na 2 CO 3 (the content of Na 2 CO 3 corresponds to 2.0 equivalents based on Fe 2+ in the aqueous ferrous sulfide solution) were mixed to produce FeCO 3 at 45°C at pH 9.8. Air was blown into the aqueous solution containing FeCO 3 at a rate of 100 ℓ per minute at 50°C for 5 hours, thereby producing goethite particles. The goethite particles produced were filtered out, washed with water and dried by an ordinary method. The goethite particles obtained were spindle-shape (a geometric standard deviation (σ g ) of 0.829) and the aspect ratio (major axial diameter:minor axial diameter) was as small as 7:1, as shown in the electron micrograph (x 30000) in Fig. 7. 〈Production of Acicular Magnetite Particles〉 Examples 15 to 28 Comparative Examples 7 to 12 Example 15 5.3 kg of the paste of the acicular goethite particles (corresponding to about 1.6 kg of acicular goethite particles) obtained in Example 1 were suspended in 28 ℓ of water. The pH of the suspension was 8.0. Thereafter, 240 ml of an aqueous solution containing 24 g of sodium hexametaphosphate (corresponding to 1.15 wt% calculated as PO 3 based on the acicular goethite particles) was added to the suspension, and the resultant mixture was stirred for 30 minutes. The resultant suspension was filtered and dried to obtain acicular goethite particles with the surfaces coated with a P compound. The thus-obtained acicular goethite particles coated with a P compound were heat-treated in air at 320°C, thereby obtaining acicular hematite particles coated (modified) with a P compound. 1000 g of the thus-obtained acicular hematite particles coated with a P compound were charged into a retort reducing vessel, and H 2 gas was blown into the particles at a rate of 2 ℓ per minute while rotating the vessel to reduce them at 360°C, thereby obtaining acicular magnetite particles coated with a P compound. It was observed through an electron microscope that the acicular magnetite particles coated with a P compound had an average major axial diameter of 0.25 µm and an aspect ratio (major axial diameter:minor axial diameter) of 7.5, and that the particle size distribution was uniform as expressed by a geometric standard deviation (σ g ) of 0.67 and no dendrites were included. When the magnetic characteristics were measured, the coercive force (Hc) was 400 Oe and the saturation magnetization (σ s ) was 82.7 emu/g. Examples 16 to 28, Comparative Examples 7 to 12 Acicular magnetite particles were obtained in the same way as in Example 15 except for varying the kind of the starting material and the heating temperature for the heat-treatment in air. The main conditions for production and the properties of the acicular magnetite particles obtained are shown in Table 3. As a result of observation through an electron microscope, all of the acicular magnetite particles obtained in Examples 16 to 28 proved to have a uniform particle size distribution and no inclusion of dendrites. 〈Production of Acicular Maghemite Particles〉 Examples 29 to 42 Comparative Examples 13 to 18 Example 29 300 g of the acicular magnetite particles coated with a P compound obtained in Example 15 were oxidized in air at 300°C for 60 minutes to obtain acicular maghemite particles coated with a P compound. It was observed through an electron microscope that the acicular maghemite particles coated with a P compound had an average major axial diameter of 0.24 µm and an aspect ratio (major axial diameter:minor axial diameter) of 7.4:1, and that the particle size distribution was uniform as expressed by a geometric standard deviation (σ g ) of 0.66 and no dendrites were included. When the magnetic characteristics were measured, the coercive force (Hc) was 371 Oe and the saturation magnetization (σ s ) was 72.2 emu/g. Examples 30 to 42, Comparative Examples 13 to 18 Acicular maghemite particles were obtained in the same way as in Example 29 except for varying the kind of acicular magnetite particles. The main conditions for production and the properties of the maghemite particles obtained are shown in Table 4. As a result of observation through an electron microscope, all of the acicular maghemite particles obtained in Examples 30 to 42 proved to have a uniform particle size distribution and no inclusion of dendrites. 〈Production of Acicular Co-Modifided Magnetite Particles〉 Examples 43 to 60 Comparative Examples 19 to 24 Example 43 100 g of the acicular magnetite particles coated with a P compound obtained in Example 15 were charged into 1.0 ℓ of water with 0.085 mol of cobalt and 0.179 mol of ferrous iron dissolved therein by using cobalt sulfate and ferrous sulfate while preventing the inclusion of air as much as possible, and dispersed until the dispersion became a fine slurry. Into the dispersion, 102 mℓ of 18-N aqueous NaOH solution was poured and water was further added so as to form 1.3 ℓ of a dispersion in which the hydroxyl concentration was 1.0 mol/ℓ. The temperature of the dispersion was raised to 100°C and it was stirred for 5 hours. Thereafter, the slurry was taken out, washed with water, filtered out and dried at 60°C to obtain acicular Co-modified magnetite particles. As a result of observation through an electron microscope, it was proved that the acicular maghemite particles obtained had the same configuration and the particle size as the precursor particles, namely, the acicular magnetite particles coated with a P compound, an average major axial diameter of 0.23 µm and an aspect ratio (major axial diameter:minor axial diameter) of 6.7:1. The particle size distribution thereof was uniform as expressed by a geometric standard deviation (σ g ) of 0.62. When the magnetic characteristics were measured, the coercive force (Hc) was 825 Oe and the saturation magnetization σs was 84.6 emu/g. Examples 44 to 60, Comparative Examples 19 to 24 Acicular magnetite particles modified by Co or Co and Fe 2+ were obtained in the same way as in Example 43 except for varying the kind of precursor particles and the amounts of Co added and Fe 2+ added under conditions that the amount of precursor magnetite particles was 100 g and the whole volume of the dispersion was 1.3 ℓ. The main conditions for production and the properties of the particles obtained are shown in Table 5. 〈Production of Acicular Co-Modifide Maghemite Particles〉 Examples 61 to 78 Comparative Examples 25 to 30 Example 61 100 g of acicular maghemite particles with the surfaces coated with a P compound obtained in Example 29 were charged into 1.0 ℓ of water with 0.085 mol of cobalt and 0.179 mol of ferrous iron dissolved therein by using cobalt sulfate and ferrous sulfate while preventing the inclusion of air as much as possible, and dispersed until the dispersion became a fine slurry. Into the dispersion, 102 mℓ of 18-N aqueous NaOH solution was poured and water was further added so as to form 1.3 ℓ of dispersion in which the hydroxyl concentration was 1.0 mol/ℓ. The temperature of the dispersion was raised to 100°C and it was stirred for 5 hours. Thereafter, the slurry was taken out, washed with water, filtered out and dried at 60°C to obtain acicular Co-modified maghemite particles. As a result of observation through an electron microscope, it was proved that the particles obtained had the same configuration and the particle size as the precursor particles, namely, the acicular maghemite particles with the surfaces coated with a P compound, an average major axial diameter of 0.22 µm and an aspect ratio (major axial diameter:minor axial diameter) of 6.6:1. The particle size distribution thereof was uniform as expressed by a geometric standard deviation (σ g ) of 0.63. When the magnetic characteristics were measured, the coercive force (Hc) was 790 Oe and the saturated magnetization (σs) was 77.0 emu/g. Examples 62 to 78, Comparative Examples 25 to 30 Acicular maghemite particles modified by Co or Co and Fe 2+ were obtained in the same way as in Example 61 except for varying the kind of the precursor particles, the amounts of Co added, Fe(II) added and NaOH added and the treating temperature and time under conditions that the amount of precursor acicular maghemite particles was 100 g and the whole volume of the dispersion was 1.3 ℓ. The main conditions for production and the properties of the particles obtained are shown in Table 6. 〈Production of Magnetic Tape〉 Examples 79 to 142 Comparative Examples 31 to 54 Example 79 A magnetic tape was produced in the following manner. A magnetic coating was prepared by charging the acicular magnetic iron oxide particles coated with a P compound obtained in Example 15, the resin and the solvents described below into a 140-cc glass bottle in the following amounts, and mixing and dispersing the above materials by a paint conditioner for 2 hours. The magnetic coating was applied to a polyethylene terephthalate film (25 µm thick) to a thickness of 40 µm by an applicator, and the film was then oriented and dried in a magnetic field of 1450 Gauss. Glass beads of 1.5 mm diameter 100 g Acicular magnetite particles 15 g Toluene 5.6 g Phosphate ester (GAFAC RE-610, produced by Toho Chemical Industrial Co., Ltd.) 0.6 g Lecithin 0.6 g Vinyl chloride-vinyl acetate copolymer (Vinilite VAGH, produced by Union Carbide) 3.75 g Butadiene acrylonitrile rubber (Hycar 1432 J, produced by Japan Geon Co., Ltd.) 0.75 g Mixed solution of Methyl isobutyl ketone, methyl ethyl ketone and toluene (3 : 1 : 1) 40.5 g The magnetic tape produced had an S.F.D. of 0.44, a coercive force (Hc) of 369 Oe, a residual flux density (Br) of 1630 Gauss and a squareness (Br/Bm) of 0.82. Examples 80 to 142, Comparative Example 31 to 54 Magnetic tapes were produced in the same way as in Example 79 except for varying the kind of magnetic particles. The acicular maghemite particles were oriented in a magnetic field of 1450 Gauss and the acicular Co-modified magnetic iron oxide particles were oriented in a magnetic field of 1900 Gauss. The properties of the magnetic tapes obtained are shown in Tables 7 to 10.

Claims: A process for producing acicular goethite particles which process comprises: (i) reacting an aqueous ferrous salt solution with less than one equivalent of an aqueous alkali hydroxide solution and/or an aqueous alkali carbonate solution based on Fe 2+ in said aqueous ferrous salt solution; (ii) blowing a molecular oxygen-containing gas into the ferrous salt reaction solution containing colloidal ferrous hydroxide or iron-containing colloidal precipitates thus obtained so as to oxidize said colloidal ferrous hydroxide or iron-containing colloidal precipitates and to produce acicular goethite nucleus particles; (iii) adding to the resultant aqueous ferrous salt reaction solution containing said acicular goethite nucleus particles not less than one equivalent of an aqueous alkali carbonate solution based on Fe 2+ in said aqueous ferrous salt reaction solution; and (iv) blowing a molecular oxygen-containing gas into the resulting mixed aqueous ferrous salt reaction solution so as to cause said goethite nucleus particles to grow. A process according to claim 1, wherein the reaction temperatures for producing goethite nucleus particles, the oxidization temperature and the reaction temperature for growing goethite nucleus particles are from 30 to 60°C. A process according to claim 1 or 2, which further comprises prior to stage (iii): (a) heat-treating the aqueous ferrous salt reaction solution containing the acicular goethite nucleus particles at a temperature of not less than 75°C and cooling the thus heat-treated solution to a temperature of less than 60°C; (b) maintaining the aqueous ferrous salt reaction solution containing the acicular goethite nucleus particles at a temperature of less than 60°C in a non-oxidizing atmosphere; or (c) heat-treating the aqueous ferrous salt reaction solution containing the acicular goethite nucleus particles at a temperature of not less than 75°C, cooling the thus heat-treated solution to a temperature of less than 60°C and maintaining the thus cooled solution in a non-oxidizing atmosphere. A process according to any one of the preceding claims for producing acicular magnetic iron oxide particles which process further comprises: (v) heat-treating in a reducing gas the thus grown acicular goethite particles or acicular hematite particles obtained by heat-treating the thus grown acicular goethite particles at 300 to 700°C, thereby producing acicular magnetite particles; and (vi) if necessary, oxidizing said acicular magnetite particles, thereby producing acicular maghemite particles. A process according to claim 4, wherein the heat-treatment in a reducing gas is carried out at from 280 to 450°C. A process according to claim 4 or 5 for producing acicular magnetic iron oxide particles which process further comprises: (vii) dispersing said acicular magnetite particles or acicular maghemite particles in an alkaline suspension containing cobalt hydroxide or cobalt hydroxide and ferrous hydroxide so that the Co content in said suspension is from 0.1 to 15.0 atomic% based on the Fe in said magnetite or maghemite particles; and (viii) heat-treating the resultant aqueous dispersion, thereby obtaining acicular magnetite particles or maghemite particles modified with Co or Co and Fe 2+ . A process according to claim 6, wherein the heat treatment (viii) is carried out at from 50 to 100°C. A process according to any one of the preceding claims, which further comprises forming a magnetic recording medium utilising the particles thus obtained.

Inventors: HARADA TOSIHARU, INABA KAZUHISA, KAWANO JUNICHI, KUROKAWA HARUKI, MORIYA TOMOHISA, SADAMURA HIDEAKI, YAMASHITA KATSUMI, HARADA, TOSIHARU, INABA, KAZUHISA, KAWANO, JUNICHI, KUROKAWA, HARUKI, MORIYA, TOMOHISA, SADAMURA, HIDEAKI, YAMASHITA, KATSUMI
Applicants: TODA KOGYO CORP, TODA KOGYO CORP.
Application year: 1991
Main classification: C01G49
IPC codes: C01G49, H01F1, G11B5