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HK1076358B - Inorganic-particle-containing additive composition, process for producing the same, and food composition containing the additive composition - Google Patents

Inorganic-particle-containing additive composition, process for producing the same, and food composition containing the additive composition Download PDF

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Publication number
HK1076358B
HK1076358B HK05108476.1A HK05108476A HK1076358B HK 1076358 B HK1076358 B HK 1076358B HK 05108476 A HK05108476 A HK 05108476A HK 1076358 B HK1076358 B HK 1076358B
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HK
Hong Kong
Prior art keywords
inorganic particles
alkali metal
weight
additive
additive composition
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HK05108476.1A
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Chinese (zh)
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HK1076358A1 (en
Inventor
北条寿一
久保田直树
森崎义政
Original Assignee
丸尾钙株式会社
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Application filed by 丸尾钙株式会社 filed Critical 丸尾钙株式会社
Priority claimed from PCT/JP2002/010659 external-priority patent/WO2003032752A1/en
Publication of HK1076358A1 publication Critical patent/HK1076358A1/en
Publication of HK1076358B publication Critical patent/HK1076358B/en

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Description

Additive composition containing inorganic particles, method for preparing the same, and food composition containing the same
Technical Field
The present invention relates to an additive composition containing inorganic particles, a method for preparing the same, and a food composition containing the same, and more particularly, to an additive composition containing inorganic particles, which can be added to foods such as yogurt, cow milk, fruit juice, milk-containing coffee (コ - ヒ - フレツシユ), powdered milk, and snack, can effectively enrich minerals, and has excellent dispersion stability and good flavor, a method for preparing the same, and a food composition containing the same.
Background
In recent years, there has been a problem of insufficient intake of calcium, magnesium, iron, and the like, and this tendency is particularly remarkable in children and the elderly who are well developed.
It goes without saying that calcium is important for bone formation and plays an important role in muscle contraction and maintaining homeostasis in the body. Magnesium has the functions of relaxing, expanding muscles and blood vessels, and the like, and is an essential mineral for human beings. When magnesium is deficient, hypertension, angina pectoris, hyperlipidemia, etc. are easily caused. Magnesium has a great relationship with calcium metabolism, and when magnesium is insufficient, various symptoms accompanied by abnormal calcium metabolism appear. Magnesium is also involved in many enzymatic reactions and is thought to maintain homeostasis in the organism.
However, in recent years, magnesium has been greatly reduced in the food finishing stage due to the eurization of the dietary pattern and the intake of grains with high whiteness, so that the dietary pattern of modern people is likely to be deficient in magnesium, and products reinforced with magnesium are receiving attention. In recent years, women who develop anemia due to iron deficiency are often seen. This tendency is particularly pronounced in women of high school and young adults. The most significant cause of such iron deficiency anemia is the problem of dietary pattern, but women are under the circumstances that iron deficiency easily causes anemia because of the increase in iron demand due to physiological bleeding and pregnancy, and insufficient intake due to weight loss, and the like, and it is generally considered that about half of women are iron deficiency. In order to solve such iron deficiency, iron-enriched foods have been sold, and many commercial products enriched with iron in milk, soft drinks, and the like have been sold.
In order to solve the above-mentioned problem of insufficient intake of various minerals, mineral-fortified foods have been sold, and attempts have been made to provide mineral-fortified cows 'milk to which minerals are further added even to cows' milk which is generally considered to have a high mineral content.
For example, in milk and yogurt, water-soluble minerals in the form of inorganic or organic acids such as calcium lactate, calcium chloride, magnesium chloride, and ferric ammonium citrate are added for the purpose of enriching the minerals; water insoluble inorganic forms of minerals such as calcium carbonate, calcium phosphate, dolomite, ferric pyrophosphate, etc. However, water-soluble minerals in the form of inorganic or organic acids tend to inhibit the stability of proteins in milk and yogurt, and it is difficult to mix them at a certain amount or more, so that there is a disadvantage that the mineral materials cannot be used in large amounts. And minerals have a unique bitter taste and thus also have problems in flavor.
On the other hand, although the water-insoluble inorganic mineral is not water-insoluble and therefore does not inhibit the stability of protein in cow's milk or yogurt, and can be used in a large amount in terms of the amount to be added, the inorganic mineral has a high specific gravity of 2.1 or more as a whole and precipitates in a short time when dispersed in cow's milk, and therefore, is not preferable in terms of food appearance, and as a result, the amount to be added is limited, and there is a disadvantage that the mineral cannot be used in a large amount.
Many methods have been proposed to compensate for the above-mentioned disadvantages and to add a large amount of calcium for food use, and for example, in Japanese patent application laid-open No. 9-9911, a method of improving dispersibility by adding at least one selected from the group consisting of phospholipids and protein decomposition products to calcium carbonate and wet-pulverizing the mixture has been proposed. However, in the method of adding phospholipids and protein decomposition products as described above, there are problems in flavor because of the peculiar odor and bitterness of phospholipids, and further, according to the above publication, since the average particle size of the calcium dispersion is 1 to 3 μm, the milk to which calcium carbonate obtained by this method is added is poor in recovery rate of calcium carbonate in a centrifugal classifier such as a clarifier in the production process of the milk, and is liable to settle in foods such as milk, and it is difficult to say that the milk is suitable for addition to foods which can be preserved for a long period of time such as milk.
Japanese patent application laid-open No. Sho 55-84327 proposes: mixing (1) a cation supply source selected from the group consisting of calcium, magnesium, iron, copper, boron, zinc, manganese, molybdenum, arsenic, silver, aluminum, barium, bismuth, mercury, nickel, lead, platinum, antimony, and tin, (2) an alkali phosphate supply source selected from the group consisting of potassium phosphate, dipotassium hydrogen phosphate, a mixture of an alkali hydroxide metal and phosphoric acid, and an alkali hydrogen phosphate metal, and (3) an organic acid having at least 3 carboxyl groups in this order of cation supply source and alkali phosphate supply source, and finally adding an organic acid source to obtain a mineral-fortified substance.
However, according to the above-mentioned publication, the effective utilization rates of various minerals are not necessarily sufficient in the dispersed state of the food additive composition produced by this method, and similarly to Japanese patent application laid-open No. Hei 9-9911, in the production process of cow milk to which the food additive composition obtained by this method is added, recovery rates of various minerals in a centrifugal classifier such as a clarifier are poor, and the cow milk is liable to settle in foods such as cow milk, and it is difficult to say that the cow milk has physical properties that can be added to foods that can be stored for a long time. There is a possibility that the content of an alkali metal salt of an organic acid having a carboxyl group or the like contained in the composition is too large, and when the food additive composition obtained by this method is added to a food, the flavor is significantly reduced due to bitterness, astringency or the like, and the value of the food is greatly impaired, and this method is not a very preferable method in terms of flavor.
Recently, with the progress of containers and storage methods for storing liquid foods such as cow milk, yogurt, and fruit juices for a long period of time, there is an increasing tendency that the foods are stored for a long period of time in shops, vending machines, and large refrigerators at home, and if calcium carbonate particles added to the same kind of foods for the purpose of calcium fortification are not well dispersed in the foods, the liquid foods are deposited on the bottom of the food containers during long-term storage, and when cow milk and fruit juice liquid foods are drunk, many of the deposits give unpleasant and unclean feelings to the drinkers.
Therefore, liquid foods which are currently sold with the aim of calcium fortification to which inorganic particles such as calcium carbonate prepared according to the conventional technique are added have such inconveniences that the inorganic particles need to be added in an extremely small amount because the dispersion stability period of the inorganic particles in the food is short, and that it needs to be limited to the range of liquid foods which are generally consumed by consumers between 1 and 2 days after purchase.
In view of the above circumstances, the present invention has been made to solve the above problems, and provides an inorganic particle-containing additive composition having excellent dispersibility and flavor as an additive for foods such as yogurt, cow milk, fruit juice, milk-containing coffee, milk powder, and snack, a method for producing the same, and a food composition obtained by adding the additive composition.
Disclosure of Invention
The first aspect of the present invention is an additive composition containing inorganic particles, which contains a polyvalent metal, a phosphate ion, an organic acid having a carboxyl group, and an alkali metal, and which has the following conditions (a) and (b):
(a)70≤X≤90000
x: the amount (mg/kg) of alkali metal contained in the solid component of the additive composition containing inorganic particles
(b)0.1≤Y≤15
Y: the additive composition containing inorganic particles was adjusted to a conductivity (mS/cm) at a solid content concentration of 10% by weight.
A second aspect of the invention is an additive composition comprising inorganic particles, characterized in that: the additive composition is prepared by a method selected from the following (I) to (IV), is composed of a composition which takes at least one phosphoric acid compound selected from calcium phosphate, magnesium phosphate and iron phosphate as a main component and contains polyvalent metal, phosphate ion, organic acid with carboxyl and alkali metal, and has the following conditions (a) and (b).
(I) A precursor material is prepared by mixing water with a polyvalent metal compound, an organic acid having a carboxyl group, and an alkali metal source, and a phosphoric acid source is added to the precursor material.
(II) mixing water with a polyvalent metal compound, a phosphoric acid source, and an alkali metal source or a phosphoric acid source/alkali metal source to prepare a precursor, and adding an organic acid having a carboxyl group to the precursor.
(III) mixing water with a polyvalent metal compound and an organic acid having a carboxyl group to prepare a precursor, and adding a phosphoric acid source and an alkali metal source to the precursor.
(IV) mixing water with a polyvalent metal compound, an organic acid having a carboxyl group and a phosphoric acid source to prepare a precursor, and adding an alkali metal source to the precursor.
(a)70≤X≤90000
X: the amount (mg/kg) of alkali metal contained in the solid component of the additive composition containing inorganic particles
(b)0.1≤Y≤15
Y: the additive composition containing inorganic particles was adjusted to a conductivity (mS/cm) at a solid content concentration of 10% by weight.
The third aspect of the present invention is an additive composition containing inorganic particles, which contains 2 to 80 parts by weight of an emulsion stabilizer relative to 100 parts by weight of the solid content of the above additive composition containing inorganic particles.
A fourth aspect of the present invention is a method for preparing an additive composition containing inorganic particles, characterized in that: a mixed slurry containing at least one phosphoric acid compound as a main component, a polyvalent metal, a phosphoric acid ion, an organic acid having a carboxyl group, and an alkali metal is prepared by a method selected from the following (I) to (IV), and then the slurry is washed.
(I) A precursor material is prepared by mixing water with a polyvalent metal compound, an organic acid having a carboxyl group, and an alkali metal source, and a phosphoric acid source is added to the precursor material.
(II) mixing water with a polyvalent metal compound, a phosphoric acid source, and an alkali metal source or a phosphoric acid source/alkali metal source to prepare a precursor, and adding an organic acid having a carboxyl group to the precursor.
(III) mixing water with a polyvalent metal compound and an organic acid having a carboxyl group to prepare a precursor, and adding a phosphoric acid source and an alkali metal source to the precursor.
(IV) mixing water with a polyvalent metal compound, an organic acid having a carboxyl group and a phosphoric acid source to prepare a precursor, and adding an alkali metal source to the precursor.
A fifth aspect of the present invention is a method for preparing an additive composition containing inorganic particles, characterized in that: the emulsion stabilizer is contained in an amount of 2 to 80 parts by weight based on 100 parts by weight of the solid content of the additive composition containing inorganic particles prepared by the above-mentioned method.
A sixth aspect of the present invention is a food composition characterized by comprising the additive composition containing inorganic particles.
Best Mode for Carrying Out The Invention
The present invention is described in detail below. In the following description, when it is not necessary to particularly distinguish between the additive slurry composition containing inorganic particles and the additive powder composition containing inorganic particles, both are referred to as inorganic particle-containing additive compositions.
The polyvalent metal compound used in the present invention includes calcium hydroxide, magnesium hydroxide, iron hydroxide, calcium oxide, magnesium oxide, iron oxide, calcium chloride, magnesium chloride, iron chloride, calcium carbonate, magnesium carbonate, iron carbonate, calcium nitrate, magnesium nitrate, iron nitrate, calcium sulfate, magnesium sulfate, iron sulfate, calcium phosphate, magnesium phosphate, iron phosphate, ferric pyrophosphate, dolomite, and the like, and it is preferable to use at least one selected from the group consisting of calcium hydroxide, magnesium hydroxide, iron hydroxide, calcium oxide, magnesium oxide, iron oxide, magnesium carbonate, calcium carbonate, iron carbonate, and dolomite, either singly or in combination of 2 or more as necessary, in order to obtain an inorganic particle-containing additive composition having a better dispersibility.
The organic acid having a carboxyl group used in the present invention includes malic acid, succinic acid, citric acid, adipic acid, fumaric acid, glutamic acid, and alkali metal salts and polyvalent metal salts thereof, and 2 or more thereof may be used alone or in combination as necessary, and in order to obtain an additive composition containing inorganic particles having a better dispersibility, at least one of citric acid, potassium citrate, sodium citrate, calcium citrate, magnesium citrate, ferric ammonium citrate, ferric citrate, and ferric sodium citrate is preferably used.
The phosphoric acid source used in the present invention includes phosphoric acid, condensed phosphoric acid and the like, and 2 or more of these may be used alone or in combination as necessary. The condensed phosphoric acid includes pyrophosphoric acid, tripolyphosphoric acid, tetrapolyphosphoric acid, pentapolyphosphoric acid, hexametaphosphoric acid, etc., and they may be used singly or in combination of 2 or more kinds.
The phosphoric acid source/alkali metal source used in the present invention includes an alkali metal of phosphoric acid and/or an alkali metal of condensed phosphoric acid, or phosphoric acid and/or condensed phosphoric acid, and an alkali metal, and more specifically, a sodium salt and a potassium salt of phosphoric acid, a sodium salt and a potassium salt of condensed phosphoric acid, a mixture of phosphoric acid and a sodium salt and a potassium salt, and a mixture of condensed phosphoric acid and a sodium salt and a potassium salt, and 2 or more kinds thereof may be used alone or in combination as necessary.
The alkali metal source used in the present invention is sodium hydroxide, potassium hydroxide, sodium oxide, potassium oxide, sodium carbonate, sodium hydrogencarbonate, potassium carbonate and potassium hydrogencarbonate, and these may be used alone or in combination of 2 or more as required.
The inorganic particle-containing additive composition of the present invention may be obtained in the form of a slurry composition, or may be obtained in the form of a powder composition by drying it to obtain a powder.
First, the additive slurry composition containing inorganic particles of the present invention is prepared by adding water and a polyvalent metal compound, an organic acid having a carboxyl group, a phosphoric acid source, and an alkali metal source to prepare a slurry. The mixing method can be roughly classified into the following methods (I), (II), (III) and (IV), and any method may be used, or 2 or more methods may be used in combination.
(I) A precursor material is prepared by mixing water with a polyvalent metal compound, an organic acid having a carboxyl group, and an alkali metal source, and a phosphoric acid source is added to the precursor material.
(II) mixing water with a polyvalent metal compound, a phosphoric acid source, and an alkali metal source or a phosphoric acid source/alkali metal source to prepare a precursor, and adding an organic acid having a carboxyl group to the precursor.
(III) mixing water with a polyvalent metal compound and an organic acid having a carboxyl group to prepare a precursor, and adding a phosphoric acid source and an alkali metal source to the precursor.
(IV) mixing water with a polyvalent metal compound, an organic acid having a carboxyl group and a phosphoric acid source to prepare a precursor, and adding an alkali metal source to the precursor.
In the above method, the method (III) or (IV) is preferably used to obtain a slurry having a better dispersibility.
In order to obtain the inorganic particle-containing additive slurry composition of the present invention, it is preferable that the molar ratio of each component in the preparation is within a specific range. That is, the polyvalent metal ion and the organic acid ion having a carboxyl group are in the range of 0.8: 1 to 20: 1, and in order to obtain an additive composition containing inorganic particles having a better dispersibility, the ratio is more preferably in the range of 1.8: 1 to 7: 1, and still more preferably in the range of 1.8: 1 to 3.5: 1.
The ratio of the organic acid ion having a carboxyl group to the phosphate ion is preferably 1: 0.6 to 1: 13.2, and in order to obtain an additive composition containing inorganic particles having a better dispersibility, the ratio is more preferably 1: 1 to 1: 5, and still more preferably 1: 1.3 to 1: 2.4. The ratio of the organic acid ion having a carboxyl group to the alkali metal ion is 1: 0.5 to 1: 8, and in order to obtain an additive composition containing inorganic particles having a better dispersibility, the ratio is more preferably 1: 1.5 to 1: 5, and still more preferably 1: 2 to 1: 4.
When the molar ratio of the polyvalent metal ion to the organic acid is less than 0.8, the dispersion state is liable to be unstable, which is not preferable; when the molar ratio exceeds 20, metal ions tend to remain in an ionic state, and therefore, when used in, for example, cow milk, the stability of protein tends to be impaired, and the protein tends to be thickened, and in extreme cases, gelation tends to cause deterioration in flavor, which is not preferable.
When the molar ratio of the phosphate ion to the organic acid is less than 0.6, the dispersion state tends to be unstable, which is not preferable; when the molar ratio exceeds 13.2, inorganic polyvalent metal aggregates tend to be easily formed, and in such a case, for example, when used in cow milk or the like, the inorganic polyvalent metal aggregates are undesirably precipitated in a large amount at the bottom of the vessel.
When the molar ratio of the alkali metal ion to the organic acid is less than 0.5, the dispersion state tends to be unstable, which is not preferable; when the molar ratio exceeds 8, the basicity tends to be too strong, and when a strong basic substance is added to various foods, the flavor tends to be impaired, which is not preferable.
The order of mixing water, the polyvalent metal compound and the organic acid having a carboxyl group is not particularly limited in the production of the precursor of the present invention. The method (III) can be further divided into the following methods (a), (b), (c) and (d) by adding a phosphoric acid source and an alkali metal source, and any of these methods can be used, or 2 or more methods can be used in combination.
(a) Adding an alkali metal phosphate and/or an alkali metal of condensed phosphoric acid;
(b) simultaneously adding alkali metal phosphate and/or alkali metal and alkali metal salt of condensed phosphoric acid;
(c) simultaneously adding phosphoric acid and/or condensed phosphoric acid and alkali metal salt;
(d) an alkali metal phosphate and/or an alkali metal of condensed phosphoric acid is added, and then an alkali metal salt is added.
The temperature at which the components are mixed to prepare the inorganic particle-containing additive slurry composition of the present invention is not particularly limited, but is preferably in the range of 1 to 70 ℃ and more preferably in the range of 10 to 40 ℃ from the viewpoint of obtaining an inorganic particle-containing additive composition having a better dispersibility. It is more preferable to mix all the components and heat the mixture to a temperature in the range of 80 to 230 ℃ because the stability over a long period of time is more easily exhibited.
When the liquid temperature during mixing exceeds 70 ℃, coarse particles tend to be formed in the liquid, and it is difficult to maintain stable dispersion characteristics for a long time, which is not preferable, and when the liquid temperature is less than 1 ℃, water as a solvent tends to freeze easily, and it tends to be difficult to obtain a composition having good dispersibility.
The additive composition containing inorganic particles of the present invention can be prepared by the following operations: namely, a slurry prepared by the method selected from the above (I) to (IV) and containing a polyvalent metal mainly composed of at least one compound selected from phosphoric acid compounds, a phosphoric acid ion, an organic acid having a carboxyl group and an alkali metal is washed. However, indispensable conditions for preparing the inorganic particle-containing additive composition of the present invention are: the amount X (mg/kg) of the alkali metal contained in the solid content of the inorganic particle-containing additive slurry and the electrical conductivity Y (mS/cm) when the inorganic particle-containing additive slurry is adjusted to a solid content concentration of 10% by weight satisfy the following conditions (a) and (b), preferably the following conditions (c) and (d), and more preferably the following conditions (e) and (f).
(a)70≤X≤90000
(b)0.1≤Y≤15
(c)70≤X≤39000
(d)0.1≤Y≤7
(e)150≤X≤10000
(f)0.25≤Y≤1.8
When the amount X (mg/kg) of the alkali metal contained in the solid component of the inorganic particle-containing additive slurry composition is less than 70, the dispersibility of the inorganic particle-containing additive composition tends to be lowered, and it is difficult not only to obtain a stable product but also to make a high concentration uneconomical; when X exceeds 90000, the metallic taste becomes strong when added to food. When the additive slurry composition containing inorganic particles is adjusted to have a conductivity Y (mS/cm) of less than 0.1 at a solid content concentration of 10% by weight, the additive composition containing inorganic particles is liable to reagglomerate, and when added to a beverage, it is difficult to obtain a stable product, and when Y exceeds 15, the flavor is reduced by bitterness, astringency, or the like when added to a food, and the taste of the food is greatly impaired.
The amount X (mg/kg) of the alkali metal contained in the solid component of the additive slurry composition containing inorganic particles in the present invention can be calculated by measurement as follows.
Measurement machine: shimadzu atomic absorption spectrophotometer AA-6700F
Preparation of a sample: the additive slurry composition containing inorganic particles was powdered, about 2g was dissolved in 3g of nitric acid, and then prepared to 100ml with distilled water to prepare a measurement sample. Further, the alkali metal may be further diluted as necessary depending on the amount of the alkali metal contained.
Solvent: distilled water
The conductivity Y (mS/cm) at the time of adjusting the inorganic particle-containing additive slurry composition of the present invention to a solid content concentration of 10% by weight can be calculated by measurement as follows.
Measurement machine: model SC82 electrical conductivity meter made by Chuanchuan
Preparation of a sample: the concentration of the solid content of the additive slurry containing inorganic particles was adjusted to 10% by weight, and this was used as a measurement sample.
Solvent: distilled water
The method for washing the additive slurry composition containing inorganic particles of the present invention is not particularly limited, and a centrifuge such as a decanter or a clarifier, a cloth type washing machine such as a spin filter, and the like can be used.
The timing for washing the inorganic particle-containing additive slurry composition of the present invention is not particularly limited, and the latter method is preferred in order to prepare an inorganic particle-containing additive slurry composition having a higher dispersibility, since the inorganic particle-containing additive slurry composition can be washed with water when the polyvalent metal, the phosphate ion, the organic acid having a carboxyl group and the alkali metal are mixed, or the polyvalent metal, the phosphate ion, the organic acid having a carboxyl group and the alkali metal are mixed, heated and washed.
The inorganic particle-containing additive slurry containing a polyvalent metal, a phosphate ion, an organic acid having a carboxyl group, and an alkali metal [ hereinafter referred to as an inorganic particle-containing additive slurry (. alpha.) ] having the conditions of the above (a) and (b) is extremely excellent in redispersibility in a liquid and long-term storage stability in a liquid, and is excellent in flavor, but in order to obtain dispersion stability in foods in an acidic region such as yogurt and dispersion stability for a longer period of time such as long-term storage of cow milk, it is preferable to produce an additive slurry containing inorganic particles [ hereinafter referred to as an inorganic particle-containing additive slurry (. beta.) ], wherein the emulsion stabilizer is contained in an amount of 2 to 80 parts by weight relative to 100 parts by weight of the solid portion of the additive slurry composition (. alpha.) containing inorganic particles.
When the content of the emulsion stabilizer is less than 2 parts by weight based on 100 parts by weight of the solid portion of the inorganic particle-containing additive slurry (α) of the present invention, it is not preferable because it is difficult to maintain emulsion stability for a long period of time and to exert a dispersion stabilizing effect on acidic foods when the inorganic particle-containing additive slurry (β) is added to foods such as canned fruit juice and yogurt in the form of beverage; on the other hand, when the amount of the compound is more than 80 parts by weight, the viscosity of the product is increased, which is not preferable in terms of texture, and the product is difficult to produce at a high concentration in terms of handling due to the increase in viscosity of the product, and is not preferable from the viewpoint of economy because the product can be produced only with a reduced concentration of the solid portion.
Examples of the emulsion stabilizer used in the present invention include gellan gum, carrageenan, sodium alginate, guar gum, karaya gum, carboxymethyl cellulose (hereinafter referred to as CMC), propylene glycol alginate (hereinafter referred to as PGA), gum arabic, tamarind gum, ghatti gum), tragacanth gum, xanthan gum, pullulan, cassia gum, locust bean gum, arabinogalactan, スクレロガム (sclerogum), condensed phosphate, sucrose stearate, sucrose palmitate, sucrose myristate, sucrose oleate, sucrose laurate and other sucrose fatty acid esters having an HLB of 8 or more, triglycerol, pentaglycerol, hexaglycerol, decaglycerol and other polyglycerol fatty acid esters having 6 to 22, preferably 14 to 18, carbon atoms of fatty acids, lecithin, modified starch, and soybean polysaccharides, and 2 or more thereof may be used alone or in combination as necessary, in order to obtain longer dispersion stability, at least one selected from sucrose fatty acid esters having HLB of 8 or more, PGA, CMC, gum arabic, arabinogalactan, condensed phosphate, polyglycerin fatty acid esters, lecithin, and modified starch is preferably used.
Further, the amount X (mg/kg) of the alkali metal contained in the solid content of the inorganic particle-containing additive slurry composition (β) of the present invention and the electrical conductivity Y (mS/cm) when the inorganic particle-containing additive slurry composition (β) is adjusted to a solid content concentration of 10% by weight preferably satisfy the conditions (a) and (b) described above, more preferably satisfy the conditions (c) and (d) described above, and still more preferably satisfy the conditions (e) and (f).
In the case of products requiring particularly long-term dispersion stability such as canned fruit juice, it is more preferable to add 2 to 80 parts by weight of an emulsion stabilizer to 100 parts by weight of the solid content of the additive slurry composition (α) containing inorganic particles, and then disperse the emulsion stabilizer by a pulverizer and/or a disperser.
The pulverizer and disperser used in the present invention are not particularly limited, and a wet pulverizer such as a ball mill, sand mill, コボ - ルミル (Kovor mill); an ultrasonic disperser, an ultrafine atomizer, an ultrafine nanoparticle processor (Nanomizer), a Microfluidizer (Microfluidizer), アルテイマイザ - (Ultimizer), an emulsifier, and a disperser.
The additive powder compositions (. alpha.) and (. beta.) containing inorganic particles can be prepared by powder-drying the additive slurry compositions (. alpha.) and (. beta.) containing inorganic particles prepared as described above. When the additive slurry composition (α) or (β) containing inorganic particles is dried, the cake-like solid matter obtained by washing may be dried as it is, or the cake-like solid matter obtained by diluting the slurry in water and slurrying the slurry again may be dried, and the latter method is preferable from the viewpoint of obtaining a dried powder having a better redispersibility. The dryer used for drying the additive slurry compositions (α) and (β) containing inorganic particles is not particularly limited, but from the viewpoint of preventing the deterioration of various surface-treating agents, it is preferable to carry out drying in an extremely short time, and from this viewpoint, a droplet spray dryer such as a spray dryer, a slurry dryer using a ceramic medium in a heated fluidized state, or a reduced pressure dryer is preferably used as the dryer.
Regarding the conditions of X and Y, the case of the inorganic particle-containing additive powder composition (. alpha.) or (. beta.) is the same as that of the above-mentioned inorganic particle-containing additive slurry composition (. alpha.) or (. beta.), that is, X is the amount of alkali metal (mg/kg) contained in the inorganic particle-containing additive composition powder, and Y is the electric conductivity Y (mS/cm) at which the inorganic particle-containing additive composition powder is adjusted to a solid content concentration of 10% by weight using water as a solvent.
The weight-average particle diameter K (μm) in the particle size distribution of the inorganic particle-containing additive composition (α) or (β) of the present invention preferably satisfies the following condition (χ), and in food applications requiring long-term storage dispersion stability, the condition (ψ) is preferably satisfied, and the condition (ω) is more preferably satisfied.
(χ)0.02≤K≤0.8
(ψ)0.02≤K≤0.3
(χ)0.02≤K≤0.1
When the weight-average particle diameter of the additive compositions (α) and (β) containing inorganic particles is larger than 0.8 μm in the particle size distribution, the additive compositions tend to settle and cannot be used for food applications which can be stored for a long period of time. On the other hand, if the average particle size is too small, the solubility of various minerals tends to increase, and for example, if the average particle size is too small, proteins and the like in cow milk tend to easily aggregate, and therefore, it is preferably 0.02 μm or more.
The weight-average particle diameter in the particle size distribution of each mineral in the additive composition (α) or (β) containing inorganic particles of the present invention is calculated by measurement under the following conditions.
Measurement machine: shimadzu corporation SA-CP4L
Preparation of a sample: the additive compositions (. alpha.,. beta.) containing inorganic particles were dropped into a solvent at 20 ℃ as described below to prepare a particle size distribution measuring sample.
Solvent: distilled water
Pre-dispersing: ultrasonic dispersion was carried out for 60 seconds using an Ultrasonic Homogenizer
Measuring temperature: 20.0 ℃ plus or minus 2.5 DEG C
When water-soluble calcium in the form of an inorganic or organic acid is added to food such as cow milk, soluble calcium ions tend to interfere with the stability of protein in cow milk, and there is a disadvantage that a certain amount or more cannot be mixed, whereas the additive composition (α) or (β) containing inorganic particles of the present invention is a composition having both an organic acid form and an inorganic acid form, and the concentration of calcium ions in the additive composition (α) or (β) containing inorganic particles is extremely low, so that the above-mentioned problem occurring when soluble calcium in the form of an inorganic or organic acid is added does not occur even when it is added to food such as cow milk.
The calcium ion concentration in the present invention is measured and calculated under the following conditions.
Measurement machine: ION METER IM-40S manufactured by east Asia electric wave industry
Preparation of a sample: the additive compositions (. alpha.,. beta.) containing inorganic particles were prepared in an amount of 10% by weight, and centrifuged at 10,000rpm for 1 hour to obtain a supernatant as a measurement sample.
Solvent: distilled water
The inorganic particle-containing additive composition (α) or (β) of the present invention is excellent in redispersibility in water, and can be easily dispersed in water without using a special disperser, stirrer or the like.
Therefore, when the inorganic particle-containing additive composition (α) or (β) of the present invention is used for producing food such as mineral-fortified milk, it is sufficient to disperse the inorganic particle-containing additive composition (α) or (β) in milk by directly adding the inorganic particle-containing additive composition (α) or (β) of the present invention to milk and vigorously stirring the mixture, and if an aqueous dispersion of minerals obtained by previously dispersing the inorganic particle-containing additive composition (α) or (β) in water is added to milk, there is no effect. In addition, the reduced milk may be prepared by adding the additive composition (α) or (β) containing inorganic particles of the present invention to cream or cream-making oil dissolved at a temperature of about 60 ℃, dispersing the mixture by high-speed stirring, adding reduced skim milk or skim milk thereto, and homogenizing the mixture.
The mineral-fortified milk and the like produced by these methods have a greatly reduced amount of minerals removed by the clarifier as compared with the case of adding minerals produced by conventional methods. That is, the minerals can be kept extremely stable in cow's milk, yogurt, and fruit juices to which the additive composition (α) or (β) containing inorganic particles of the present invention is added. Since the inorganic particle-containing additive composition (α) or (β) of the present invention has good mineral dispersibility, it can be added to milk or the like with a short stirring time, and therefore, mineral aggregation which is visible when stirred for a long time in cream does not occur. In addition, the additive composition (α) or (β) containing inorganic particles of the present invention does not cause a unique flavor or odor due to a water-soluble calcium agent and gelation of a product even when added in a large amount to cow milk, milk-containing coffee, or the like, and does not affect the flavor or texture of the product.
The inorganic particle-containing additive composition (α) or (β) of the present invention may be used for the purpose of mineral fortification in liquid foods such as cream, soup, coffee, black tea, oolong tea, soybean milk, sports drinks, and near-water drinks (for the purpose of mineral fortification; alcoholic beverages such as wine and liquor; cheese, chewing gum, bread, snack, flour, and other food products or tablets.
The amount of the inorganic particle-containing composition (. alpha.,. beta.) of the present invention is not particularly limited, but 1 to 1000mg of calcium, 0.5 to 500mg of magnesium, and 0.1 to 20mg of iron are preferably added to various foods, more preferably 5 to 500mg of calcium, 2.5 to 250mg of magnesium, and 0.1 to 10mg of iron are added, and still more preferably 10 to 300mg of calcium, 5 to 150mg of magnesium, and 0.1 to 5mg of iron are added.
The additive composition (alpha) or (beta) containing inorganic particles of the present invention is used in combination with mineral salts in water-soluble inorganic form such as calcium lactate, calcium chloride, magnesium sulfate, magnesium chloride, sodium ferric citrate, ammonium ferric citrate, etc., without any problem.
The present invention will be described in more detail below with reference to examples and comparative examples, but the present invention is not limited to these examples.
Example 1
The parent material was prepared by mixing 1142.9g of water and 155.4g of calcium hydroxide, 192g of citric acid (anhydrous) and 343g of 40% phosphoric acid with stirring. Then, 224g of 50% potassium hydroxide was added to the precursor, sufficiently stirred, and heated at 120 ℃ for 30 minutes in an autoclave to obtain a mixed slurry.
The slurry mixture was dewatered by an ultracentrifuge GLE type (CEPA Co., Ltd.), and the dewatered cake was redispersed in water to give an additive slurry composition (. alpha.) containing inorganic particles having a solid content of 35% by weight.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 2.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 65,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 12.5.
The weight-average particle size of the particle size distribution in the additive slurry composition containing inorganic particles was 0.15. mu.m. The calcium ion concentration of the additive slurry composition containing inorganic particles was 0 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Example 2
The parent material was prepared by mixing 1142.9g of water with 155.4g of calcium hydroxide and 192g of citric acid (anhydrous) with stirring. 609.6g of 40% dipotassium hydrogenphosphate was added to the parent substance and stirred, and finally 56g of 50% potassium hydroxide was added thereto, and stirred well, followed by heating at 120 ℃ for 30 minutes in an autoclave to obtain a mixed slurry.
Subsequently, the mixed slurry was dewatered by an ultracentrifuge, and the dewatered cake was redispersed in water to prepare an additive slurry composition (α) containing inorganic particles having a solid content concentration of 35% by weight.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 3.3.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 88,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 14.3.
The weight-average particle diameter in the particle size distribution of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition was 0.14. mu.m. The calcium ion concentration of the additive slurry composition containing inorganic particles was 0 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Example 3
The parent material was prepared by mixing 1142.9g of water with 155.4g of calcium hydroxide, 192g of citric acid (anhydrous) and 224g of 50% potassium hydroxide with stirring. Then, 343g of 40% phosphoric acid was added to the precursor, and the mixture was sufficiently stirred and heated at 120 ℃ for 30 minutes in an autoclave to obtain a mixed slurry composition.
The mixed slurry was dewatered by an ultracentrifuge, and the dewatered cake was redispersed in water to prepare an additive slurry composition (α) containing inorganic particles having a solid content concentration of 35% by weight.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 2.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 59,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 11.3.
The weight-average particle diameter in the particle size distribution of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition was 0.15. mu.m. The calcium ion concentration of the additive slurry composition containing inorganic particles was 0 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Example 4
The parent material was prepared by mixing 1142.9g of water and 155.4g of calcium hydroxide, 224g of 50% potassium hydroxide and 343g of 40% phosphoric acid with stirring. 192g of citric acid (anhydrous) was added to the precursor, sufficiently stirred, and heated at 120 ℃ for 30 minutes in an autoclave to obtain a mixed slurry.
The mixed slurry was dewatered by a rotary filter, and the dewatered cake was redispersed in water to prepare an additive slurry composition (α) containing inorganic particles having a solid content concentration of 35% by weight.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 2.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 70,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 13.4.
The weight-average particle diameter in the particle size distribution of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition was 0.31. mu.m. The calcium ion concentration of the additive slurry composition containing inorganic particles was 0.2 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Example 5
The parent material was prepared by mixing 1142.9g of water with 155.4g of calcium hydroxide and 192g of citric acid (anhydrous) with stirring. Subsequently, 743g of 40% tripotassium phosphate was added to the base material, and the mixture was sufficiently stirred to obtain a mixed slurry.
The mixed slurry was dewatered by a rotary filter, the dewatered cake was redispersed in water, dewatered by a rotary filter again, and redispersed in water to give an additive slurry (α) containing inorganic particles having a solid content concentration of 35% by weight.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 4.2.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 35,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 6.0.
The weight-average particle diameter in the particle size distribution of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition was 0.39 μm, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.5 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Example 6
The parent material was prepared by mixing 1142.9g of water and 155.4g of calcium hydroxide, 192g of citric acid (anhydrous) and 343g of 40% phosphoric acid with stirring. Then, 224g of 50% potassium hydroxide was added to the precursor, and the mixture was sufficiently stirred to obtain a mixed slurry. Subsequently, the slurry composition was dewatered by an ultracentrifuge, the dewatered cake was redispersed in water again, and the slurry was heated at 120 ℃ for 30 minutes by an autoclave to obtain an additive slurry (α) containing inorganic particles having a solid content of 35% by weight.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 2.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 53,000, and the conductivity Y (mS/cm) at a solid content concentration of 10% by weight was 9.5.
The weight-average particle diameter in the particle size distribution of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition was 0.30. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.2 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Example 7
The parent material was prepared by mixing 1142.9g of water and 155.4g of calcium hydroxide, 192g of citric acid (anhydrous) and 343g of 40% phosphoric acid with stirring. Then, 224g of 50% potassium hydroxide was added to the precursor, sufficiently stirred, and heated at 120 ℃ for 30 minutes in an autoclave to obtain a mixed slurry.
The slurry mixture was dewatered by an ultracentrifuge, and the dewatered cake was redispersed in water, dewatered by an ultracentrifuge, and redispersed in water again to give an additive slurry composition (α) containing inorganic particles having a solid content of 35% by weight.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 2.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 22,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 3.5.
The weight-average particle diameter in the particle size distribution of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition was 0.12. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.5 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Example 8
The same operation as in example 7 was carried out except that the slurry was dehydrated by an ultracentrifuge and redispersion was repeated 3 times, to obtain an additive slurry (. alpha.) containing inorganic particles and having a solid content of 35% by weight.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 2.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 8,300, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 1.2.
The weight-average particle diameter in the particle size distribution of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition was 0.13. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.7 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Example 9
An inorganic particle-containing additive slurry (. alpha.) having a solid content of 35% by weight was prepared in the same manner as in example 7, except that the molar ratio of the components during the reaction was changed as follows.
The molar ratio of the components in the reaction is 6.7: 1.0: 4.4: 3.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 7,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 1.5.
The weight-average particle diameter in the particle size distribution of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition was 0.30. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.9 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Example 10
An inorganic particle-containing additive slurry (. alpha.) having a solid content of 35% by weight was prepared in the same manner as in example 7, except that the molar ratio of the components during the reaction was changed as follows.
The molar ratio of the components in the reaction is 13.5: 1.0: 8.8: 3.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 4,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 0.9.
The weight-average particle diameter in the particle size distribution of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition was 0.35. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 1.0 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Example 11
An additive slurry (. alpha.) containing inorganic particles having a solid content of 35% by weight was obtained in the same manner as in example 7, except that calcium oxide was used in place of calcium hydroxide.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 2.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 36,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 6.6.
The weight-average particle diameter in the particle size distribution of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition was 0.47. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 1.0 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Example 12
An inorganic particle-containing additive slurry (. alpha.) having a solid content concentration of 35% by weight was obtained in the same manner as in example 8, except that calcium carbonate was used in place of calcium hydroxide.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 2.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 9,400, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 1.6.
The weight-average particle diameter in the particle size distribution of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition was 0.13. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.8 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Example 13
An additive slurry (. alpha.) containing inorganic particles having a solid content of 35% by weight was obtained in the same manner as in example 7 except that 81.4g of calcium hydroxide and 58.3g of magnesium hydroxide were used in place of 155.4g of calcium hydroxide.
The molar ratio of the components in the reaction is 1.1: 1.0: 1.4: 2.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 31,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 5.6.
The weight-average particle diameter in the particle size distribution of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition was 0.28. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.5 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Example 14
An additive slurry (. alpha.) containing inorganic particles having a solid content of 35% by weight was obtained in the same manner as in example 7, except that 151.7g of calcium hydroxide and 4.5g of ferrous hydroxide were used in place of 155.4g of calcium hydroxide.
The molar ratio of the components in the reaction is 2.05: 0.05: 1.0: 1.4: 2.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 37,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 6.8.
The weight-average particle diameter in the particle size distribution of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition was 0.26. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.9 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Example 15
An additive slurry (. alpha.) containing inorganic particles having a solid content of 35% by weight was obtained in the same manner as in example 7 except that 112g of 50% potassium hydroxide and 80g of 50% sodium hydroxide were used in place of 224g of 50% potassium hydroxide.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 1.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 16,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 2.7.
The weight-average particle diameter in the particle size distribution of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition was 0.17. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.5 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Example 16
The additive slurry (. alpha.) containing inorganic particles obtained in example 7 was dried by a spray dryer to obtain an additive powder containing inorganic particles. To 100 parts by weight of the additive powder containing inorganic particles, 20 parts by weight of pentaglycerol monostearate and water were added, and they were mixed with stirring to prepare an additive slurry composition (β) containing inorganic particles having a solid content concentration of 35% by weight.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 18,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 2.9.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.10. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.4 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity. Further, pentaglycerol monostearate was dissolved in hot water at 70 ℃ and then added.
Example 17
The additive slurry (. alpha.) containing inorganic particles obtained in example 7 was dried by a spray dryer to obtain an additive powder containing inorganic particles. To 100 parts by weight of the additive powder containing inorganic particles, 8 parts by weight of gum arabic and water were added, and stirred and mixed to prepare an additive slurry composition (β) containing inorganic particles having a solid content concentration of 35% by weight.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 21,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 3.4.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.08 μm, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.3 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity. The gum arabic is added after being dissolved in water in advance.
Example 18
To 100 parts by weight of the inorganic particle-containing additive slurry (. alpha.) obtained in example 7, 12 parts by weight of propylene glycol alginate was added, and the mixture was stirred and mixed to prepare an inorganic particle-containing additive slurry (. beta.) having a solid content concentration of 21% by weight.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 20,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 3.2.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.11. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.2 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity. The propylene glycol alginate was dissolved in hot water at 70 ℃ and then added.
Example 19
The additive slurry (. alpha.) containing inorganic particles obtained in example 1 was dried by a spray dryer to obtain an additive powder containing inorganic particles. Sucrose stearate 15 parts by weight and water were added to 100 parts by weight of the additive powder containing inorganic particles, and they were mixed with stirring to prepare an additive slurry composition (. beta.) containing inorganic particles having a solid content concentration of 35% by weight.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 62,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 11.6.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.10. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.2 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity. Sucrose stearate was dissolved in hot water at 70 ℃ and added.
Example 20
The additive slurry composition containing inorganic particles obtained in example 7 was dried by a spray dryer to obtain an additive powder containing inorganic particles. Adding 10 weight parts of propylene glycol alginate and water to 100 weight parts of additive powder containing inorganic particles, stirring and mixingThen, a mixed slurry having a solid content concentration of 30% by weight was prepared, and then the mixed slurry was stirred at a rate of 150kg/cm2Was dispersed by a high-pressure homogenizer (manufactured by gaulin corporation) under the pressure of (1) to obtain an additive slurry composition (β) containing inorganic particles.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 20,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 3.2.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.04. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.3 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity. The propylene glycol alginate was dissolved in hot water at 70 ℃ and then added.
Example 21
The additive slurry composition containing inorganic particles obtained in example 7 was dried by a spray dryer to obtain an additive powder containing inorganic particles. To 100 parts by weight of the inorganic particle-containing additive powder, 20 parts by weight of pentaglycerol monostearate and water were added, and the mixture was stirred and mixed to prepare a mixed slurry having a solid content concentration of 35% by weight, followed by wet pulverization using a wet pulverizer KD-oriented Dyno mill (manufactured by WAB corporation), to obtain an inorganic particle-containing additive slurry composition (β).
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 18,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 2.9.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.06. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.2 mg/l.
The resulting additive slurry containing inorganic particles had a very low viscosity and no problems at all with regard to flowability. Further, pentaglycerol monostearate was previously dissolved in hot water at 70 ℃ and then added.
Example 22
The additive slurry (. alpha.) containing inorganic particles obtained in example 10 was dried by a spray dryer to obtain an additive powder containing inorganic particles. To 100 parts by weight of the inorganic particle-containing additive powder, 20 parts by weight of pentaglycerol monostearate and water were added, and the mixture was stirred and mixed to prepare a mixed slurry having a solid content concentration of 35% by weight, followed by wet pulverization using a wet pulverizer KD-oriented Dyno mill (manufactured by WAB corporation), to obtain an inorganic particle-containing additive slurry composition (β).
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 4,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 1.0.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.15. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.2 mg/l.
The resulting additive slurry containing inorganic particles had a very low viscosity and no problems at all with regard to flowability. Further, pentaglycerol monostearate was previously dissolved in hot water at 70 ℃ and then added.
Comparative example 1
An additive slurry composition containing inorganic particles having a solid content of 23% by weight was obtained in the same manner as in example 1, except that the step after the dewatering in an ultracentrifuge was not carried out.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 2.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 108,000, and the conductivity Y (mS/cm) at a solid content concentration of 10% by weight was 17.5.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.18. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.1 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Comparative example 2
An additive slurry composition containing inorganic particles having a solid content of 23% by weight was obtained in the same manner as in example 2, except that the step after the dewatering in the ultracentrifuge was not carried out.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 3.3.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 248,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 40.2.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.14. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.2 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Comparative example 3
An additive slurry containing inorganic particles having a solid content of 22% by weight was obtained in the same manner as in example 5, except that the step after the dewatering in the ultracentrifuge was not carried out.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 275,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 45.0.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.15. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.6 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Comparative example 4
An additive slurry containing inorganic particles having a solid content of 23% by weight was obtained in the same manner as in example 11, except that the step after the dewatering in the ultracentrifuge was not carried out.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 2.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 158,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 24.7.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.51. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.8 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Comparative example 5
An additive slurry containing inorganic particles having a solid content of 23% by weight was obtained in the same manner as in example 12, except that the step after the dewatering in the ultracentrifuge was not carried out.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 2.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 98,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 16.3.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.16. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.3 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Comparative example 6
The procedure of example 13 was repeated in the same manner except that the step after the dehydration in the ultracentrifuge was not carried out to obtain an additive slurry containing inorganic particles having a solid content of 23% by weight.
The molar ratio of the components in the reaction is 1.1: 1.0: 1.4: 2.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 111,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 17.9.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.31. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.5 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Comparative example 7
An additive slurry containing inorganic particles having a solid content of 23% by weight was obtained in the same manner as in example 14, except that the step after the dewatering in the ultracentrifuge was not carried out.
The molar ratio of the components in the reaction is 2.05: 0.05: 1.0: 1.4: 2.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 173,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 26.4.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.29. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.3 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Comparative example 8
An additive slurry containing inorganic particles having a solid content of 22% by weight was obtained in the same manner as in example 15, except that the step after the dewatering in the ultracentrifuge was not carried out.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 1.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 107,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 16.7.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.23. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.2 mg/l.
The resulting additive slurry composition containing inorganic particles had a very low viscosity and had no problem at all with respect to fluidity.
Comparative example 9
An additive slurry containing inorganic particles was obtained in the same manner as in example 1 except that the slurry was dehydrated by an ultracentrifuge and redispersed repeatedly 10 times, and the solid content concentration was 15% by weight.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 2.0.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 60, and the conductivity Y (mS/cm) at the time of adjusting the solid content concentration to 10% by weight was 0.15.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 1.24. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 2.7 mg/l.
The obtained additive slurry composition containing inorganic particles had a sticky property and was inferior in workability.
Comparative example 10
An additive slurry containing inorganic particles having a solid content of 15% by weight was obtained in the same manner as in example 5, except that the slurry was dehydrated by an ultracentrifuge and redispersed repeatedly 12 times.
The molar ratio of the components in the reaction is 2.1: 1.0: 1.4: 4.2.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 90, and the conductivity Y (mS/cm) at a solid content concentration of 10% by weight was 0.08.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 1.09. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 2.1 mg/l.
The obtained additive slurry composition containing inorganic particles had a sticky property and was inferior in workability.
Comparative example 11
The additive slurry composition containing inorganic particles obtained in comparative example 1 was dried by a spray dryer to obtain an additive powder containing inorganic particles. To 100 parts by weight of the inorganic particle-containing additive powder, 20 parts by weight of pentaglycerol monostearate and water were added, and they were mixed with stirring to prepare an inorganic particle-containing additive slurry composition having a solid content concentration of 35% by weight.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 95,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 15.6.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.15. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.2 mg/l.
The resulting additive slurry composition containing a high concentration of inorganic particles had a very low viscosity and had no problem at all with regard to fluidity. Further, pentaglycerol monostearate was previously dissolved in hot water at 70 ℃ and then added.
Comparative example 12
An additive slurry composition containing inorganic particles having a solid content of 35% by weight was obtained in the same manner as in comparative example 11, except that gum arabic was added in an amount of 8 parts by weight per 100 parts by weight of the additive powder containing inorganic particles.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 103,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 16.9.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.11. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.2 mg/l.
The resulting additive slurry composition containing a high concentration of inorganic particles had a very low viscosity and had no problem at all with regard to fluidity. The gum arabic is dissolved in water in advance and then added.
Comparative example 13
The additive slurry composition containing inorganic particles obtained in comparative example 1 was dried by a spray dryer to obtain an additive powder containing inorganic particles. Adding 10 parts by weight of propylene glycol alginate and water to 100 parts by weight of the additive powder containing inorganic particles, stirring and mixing to prepare a mixed slurry having a solid content concentration of 35% by weight, and adding the mixed slurry to a mixing tank at a concentration of 150kg/cm2Is dispersed by a homogenizer to obtain an additive slurry composition containing inorganic particles.
After the additive slurry composition containing the inorganic particles was dried, the amount X (mg/kg) of the alkali metal contained in the solid content was 105,000, and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight was 17.2.
The weight-average particle diameter of the inorganic particle-containing additive in the inorganic particle-containing additive slurry composition in the particle size distribution was 0.05. mu.m, and the calcium ion concentration of the inorganic particle-containing additive slurry composition was 0.3 mg/l.
The resulting additive slurry composition containing a high concentration of inorganic particles had a very low viscosity and had no problem at all with regard to fluidity. The propylene glycol alginate was dissolved in hot water at 70 ℃ and then added.
TABLE 1
Polyvalent Metal Compound A Organic acid B Phosphoric acid source C Alkali metal compound D Molar ratio of A to B C/B molar ratio D/B molar ratio Emulsion stabilizer Amount of alkali metal X (mg/kg) Conductivity Y (mS/cm) Weight average particle diameter K (μm) Preparation method
Example 1 Ca(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 - 65,000 12.5 0.15 IV
Example 2 Ca(OH)2 Citric acid Dipotassium hydrogen phosphate KOH 2.1∶1 1.4∶1 3.3∶1 - 88,000 14.3 0.14 III
Example 3 Ca(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 - 59,000 11.3 0.15 I
Example 4 Ca(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 - 70,000 13.4 0.31 II
Example 5 Ca(OH)2 Citric acid Tripotassium phosphate - 2.1∶1 1.4∶1 4.2∶1 - 35,000 6.0 0.39 III
Example 6 Ca(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 - 53,000 9.5 0.30 IV
Example 7 Ca(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 - 22,000 3.5 0.12 IV
Example 8 Ca(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 - 8,300 1.2 0.13 IV
Example 9 Ca(OH)2 Citric acid Phosphoric acid KOH 6.7∶1 4.4∶1 3.0∶1 - 7,000 1.5 0.30 IV
Example 10 Ca(OH)2 Citric acid Phosphoric acid KOH 13.5∶1 8.8∶1 3.0∶1 - 4,000 0.9 0.35 IV
Example 11 CaO Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 - 36,000 6.6 0.47 IV
Example 12 CaCO3 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 - 9,400 1.6 0.13 IV
Example 13 Ca(OH)2Mg(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 - 31,000 5.6 0.28 IV
Example 14 Ca(OH)2Fe(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 - 37,000 6.8 0.26 IV
Example 15 Ca(OH)2 Citric acid Phosphoric acid KOHNaOH 2.1∶1 1.4∶1 2.0∶1 - 16,000 2.7 0.17 IV
Example 16 Ca(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 PG 18,000 2.9 0.10 IV
Example 17 Ca(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 AG 21,000 3.4 0.08 IV
Example 18 Ca(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 PGA 20,000 3.2 0.11 IV
Example 19 Ca(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 SE 62,000 11.6 0.10 IV
Example 20 Ca(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 20∶1 PGA 20,000 3.2 0.04 IV
Example 21 Ca(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 20∶1 PG 18,000 2.9 0.06 IV
Example 22 Ca(OH)2 Citric acid Phosphoric acid KOH 13.5∶1 8.8∶1 3.0∶1 PG 4,000 1.0 0.15 IV
PG: abbreviation for pentaglycerol monostearate
AG: abbreviation of gum arabic
PGA: abbreviation for propylene glycol alginate
And SE: abbreviation for sucrose stearate
TABLE 2
Polyvalent Metal Compound A Organic acid B Phosphoric acid source C Alkali metal compound D Molar ratio of A to B C/B molar ratio D/B molar ratio Emulsion stabilizer Amount of alkali metal X (mg/kg) Conductivity Y (mS/cm) Weight average particle diameter K (μm) Preparation method
Comparative example 1 Ca(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 - 108,000 17.5 0.18 IV
Comparative example 2 Ca(OH)2 Citric acid Dipotassium hydrogen phosphate KOH 2.1∶1 1.4∶1 3.3∶1 - 248,000 40.2 0.14 III
Comparative example 3 Ca(OH)2 Citric acid Tripotassium phosphate - 2.1∶1 1.4∶1 4.2∶1 - 275,000 45.0 0.15 III
Comparative example 4 CaO Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 - 158,000 24.7 0.51 IV
Comparative example 5 CaCO3 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 - 98,000 16.3 0.16 IV
Comparative example 6 Ca(OH)2Mg(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 - 111,000 17.9 0.31 IV
Comparative example 7 Ca(OH)2Fe(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 - 173,000 26.4 0.29 IV
Comparative example 8 Ca(OH)2 Citric acid Phosphoric acid KOHNaOH 2.1∶1 1.4∶1 2.0∶1 - 107,000 16.7 0.23 IV
Comparative example 9 Ca(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 - 60 0.15 1.24 IV
Comparative example 10 Ca(OH)2 Citric acid Tripotassium phosphate - 2.1∶1 1.4∶1 4.2∶1 - 90 0.08 1.09 III
Comparative example 11 Ca(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 PG 95,000 15.6 0.15 IV
Comparative example 12 Ca(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 AG 103,000 16.9 0.11 IV
Comparative example 13 Ca(OH)2 Citric acid Phosphoric acid KOH 2.1∶1 1.4∶1 2.0∶1 PGA 105,000 17.2 0.05 IV
PG: abbreviation for pentaglycerol monostearate
AG: abbreviation of gum arabic
PGA: abbreviation for propylene glycol alginate
Examples 23 to 44 and comparative examples 14 to 26
The additive slurry compositions containing inorganic particles obtained in examples 1 to 22 and comparative examples 1 to 13 were dried by a spray dryer to obtain additive powder compositions containing inorganic particles.
Next, water was added to the additive powder compositions containing inorganic particles obtained in examples 23 to 44 to adjust the solid content to 35%, and the mixture was shaken with a shaker for 10 minutes to prepare redispersions. The viscosity of the redispersion of the additive powder composition containing inorganic particles obtained was substantially the same as that of the additive slurry composition containing inorganic particles before drying, and there was no problem at all in fluidity. The amount X (mg/kg) of the alkali metal contained in the solid content of the redispersion liquid after drying and the conductivity Y (mS/cm) when the solid content concentration was adjusted to 10% by weight are shown in Table 3.
TABLE 3
X Y X Y X Y X Y
Example 23 65,000 12.4 Example 24 88,000 14.3 Example 25 59,000 11.5 Example 26 71,000 13.7
Example 27 34,000 6.2 Example 28 54,000 9.7 Example 29 22,000 3.4 Example 30 8,300 1.2
Example 31 7,000 1.5 Example 32 4,000 1.0 Example 33 36,000 6.5 Example 34 9,300 1.4
Example 35 32,000 5.7 Example 36 37,000 6.7 Example 37 15,000 2.5 Example 38 18,000 2.9
Example 39 21,000 3.4 Example 40 20,000 3.2 EXAMPLE 41 62,000 11.4 Example 42 20,000 3.1
Example 43 18,000 3.0 Example 44 4,000 1.0
X: amount of alkali Metal (mg/kg)
Y: conductivity Y (mS/cm)
Next, water was added to the additive powder compositions containing inorganic particles obtained in comparative examples 14 to 26 so that the solid content concentration was the same as the solid content concentration of each slurry before pulverization, and the mixture was shaken for 10 minutes by a shaker to prepare redispersions. The viscosity of the redispersion of the additive powder composition containing inorganic particles was substantially the same as that of the additive slurry composition containing inorganic particles before drying, and there was no problem at all in fluidity. The amount X (mg/kg) of the alkali metal contained in the solid content of the redispersion liquid after drying and the conductivity Y (mS/cm) at which the solid content concentration was adjusted to 10% by weight are shown in Table 4
TABLE 4
X Y X Y X Y
Comparative example 14 107,000 17.7 Comparative example 15 249,000 40.8 Comparative example 16 276,000 45.1
Comparative example 17 157,000 24.6 Comparative example 18 97,000 16.1 Comparative example 19 110,000 17.2
Comparative example 20 172,000 26.1 Comparative example 21 107,000 16.4 Comparative example 22 60 0.14
Comparative example 23 90 0.08 Comparative example 24 94,000 15.3 Comparative example 25 103,000 16.6
Comparative example 26 105,000 17.0
X: amount of alkali Metal (mg/kg)
Y: conductivity Y (mS/cm)
Example 45
The additive slurry containing inorganic particles prepared in example 1 was measured, the total amount of calcium was adjusted to 32g, and the slurry was dispersed in 200g of cream dissolved at 60 ℃, and then added to 9.55kg of skim milk and stirred, followed by sterilization, to obtain calcium-fortified milk. The mineral-enriched milk was put into a plurality of 100ml measuring cylinders, stored at 5 ℃, and the milk in the measuring cylinders was periodically and gently poured out, and the change with time of the amount of the sediment remaining in the bottom of the measuring cylinders was visually observed. The results are reported in table 5 as the following 5-level representation. The calcium-fortified milk was subjected to sensory tests on 10 men and women, and the flavor was evaluated on a 5-point scale, and the average value thereof is also shown in table 5.
(amount of precipitate)
Hardly confirmed 5
Minute amount of precipitate 4 was confirmed
A small amount of precipitate 3 was confirmed
It was confirmed that there was much precipitation 2
A large amount of precipitate 1 was confirmed
(flavor)
Good flavor 7
Flavor is not abnormal 6
Flavor hardly had abnormality 5
Slight abnormality (slightly different feeling) in flavor 4
Poor flavor (unpleasant feeling) 3
Poor flavor (strong unpleasant feeling) 2
Very poor flavor (very strong unpleasant feeling) 1
Examples 46 to 84 and comparative examples 27 to 52
Mineral-fortified milk was obtained in the same manner as in example 45, except that the additive slurry compositions containing inorganic particles or the powder compositions thereof prepared in examples 2 to 44 and comparative examples 1 to 26 were used and the total weight of the mineral content was adjusted to the same concentration as in example 45. The observation of the precipitates and the taste sensation test of these mineral-fortified milks were carried out in the same manner as in example 45. The results are shown in tables 5 and 6.
TABLE 5
The additive slurry composition or powder composition containing inorganic particles Amount of precipitate Flavor (I) and flavor (II)
After 3 days After 7 days After 14 days
Example 45 Composition prepared according to example 1 5 5 5 5
Example 46 Composition prepared according to example 2 5 5 5 4
Example 47 Composition prepared according to example 3 5 5 5 5
Example 48 Composition prepared according to example 4 5 4 4 4
Example 49 Composition prepared according to example 5 4 3 3 6
Example 50 Composition prepared according to example 6 5 4 4 5
Example 51 Composition prepared according to example 7 5 5 5 6
Example 52 Composition prepared according to example 8 5 5 4 7
Example 53 Composition prepared according to example 9 4 4 4 7
Example 54 Composition prepared according to example 10 4 3 3 7
Example 55 Composition prepared according to example 11 4 3 3 5
Example 56 Composition prepared according to example 12 5 5 4 7
Example 57 Composition prepared according to example 13 5 5 4 6
Example 58 Composition prepared according to example 14 5 5 4 6
Example 59 Composition prepared according to example 15 5 5 4 6
Example 60 Composition prepared according to example 16 5 5 5 6
Example 61 Composition prepared according to example 17 5 5 5 6
Example 62 Composition prepared according to example 18 5 5 5 6
Example 63 Composition prepared according to example 19 5 5 5 5
Example 64 Composition prepared according to example 20 5 5 5 6
Example 65 Composition prepared according to example 21 5 5 5 6
Example 66 Composition prepared according to example 22 5 4 4 7
Example 67 Composition prepared according to example 23 5 5 5 5
Example 68 Composition prepared according to example 24 5 5 5 4
Example 69 Composition prepared according to example 25 5 5 5 5
Example 70 Composition prepared according to example 26 5 4 4 4
Example 71 Composition prepared according to example 27 4 3 3 6
Example 72 Composition prepared according to example 28 5 4 4 5
Example 73 Composition prepared according to example 29 5 5 5 6
Example 74 Composition prepared according to example 30 5 5 4 7
Example 75 Composition prepared according to example 31 4 4 4 7
Example 76 Composition prepared according to example 32 4 3 3 7
Example 77 Composition prepared according to example 33 4 3 3 5
Example 78 Composition prepared according to example 34 5 5 4 7
Example 79 Composition prepared according to example 35 5 5 4 6
Example 80 Composition prepared according to example 36 5 5 4 6
Example 81 Composition prepared according to example 37 5 5 4 6
Example 82 Composition prepared according to example 38 5 5 5 6
Example 83 Composition prepared according to example 39 5 5 5 6
Example 84 Composition prepared according to example 40 5 5 5 6
Example 85 Composition prepared according to example 41 5 5 5 5
Example 86 Composition prepared according to example 42 5 5 5 6
Example 87 Composition prepared according to example 43 5 5 5 6
Example 88 Composition prepared according to example 44 5 4 4 7
TABLE 6
The additive slurry composition or powder composition containing inorganic particles Amount of precipitate Flavor (I) and flavor (II)
After 3 days After 7 days l4 days later
Comparative example 27 Composition prepared according to comparative example 1 5 5 5 3
Comparative example 28 Composition prepared according to comparative example 2 5 5 5 1
Comparative example 29 Composition prepared according to comparative example 3 5 5 5 1
Comparative example 30 Composition prepared according to comparative example 4 4 3 3 2
Comparative example 31 Composition prepared according to comparative example 5 5 5 4 3
Comparative example 32 Composition prepared according to comparative example 6 4 4 4 3
Comparative example 33 Composition prepared according to comparative example 7 5 4 4 2
Comparative example 34 Composition prepared according to comparative example 8 5 5 4 3
Comparative example 35 Composition prepared according to comparative example 9 2 1 1 4
Comparative example 36 Composition prepared according to comparative example 10 2 1 1 4
Comparative example 37 Composition prepared according to comparative example 11 5 5 5 3
Comparative example 38 Composition prepared according to comparative example 12 5 5 5 3
Comparative example 39 Composition prepared according to comparative example 13 5 5 5 3
Comparative example 40 Composition prepared according to comparative example 14 5 5 5 3
Comparative example 41 Composition prepared according to comparative example 15 5 5 5 1
Comparative example 42 Composition prepared according to comparative example 16 5 5 5 1
Comparative example 43 Composition prepared according to comparative example 17 4 3 3 2
Comparative example 44 Composition prepared according to comparative example 18 5 5 4 3
Comparative example 45 Composition prepared according to comparative example 19 4 4 4 3
Comparative example 46 Composition prepared according to comparative example 20 5 4 4 2
Comparative example 47 Composition prepared according to comparative example 21 5 5 4 3
Comparative example 48 Composition prepared according to comparative example 22 2 1 1 4
Comparative example 49 Composition prepared according to comparative example 23 2 1 1 4
Comparative example 50 Composition prepared according to comparative example 24 5 5 5 3
Comparative example 51 Composition prepared according to comparative example 25 5 5 5 3
Comparative example 52 Composition prepared according to comparative example 26 5 5 5 3
Example 89
The additive slurry composition containing inorganic particles prepared in example 2 was measured so that the amount of calcium was 32g, 2.5kg of commercially available cow milk, 100g of cream, and 1.45kg of skim milk were added to 5kg of water and stirred uniformly, sterilized and cooled according to a conventional method, and then 200g of a starter prepared in advance was inoculated, fermented at 38 ℃ for 5 hours, stirred, and homogenized to obtain calcium-fortified yogurt in the form of a beverage.
The sensory test of this yogurt was carried out in the same manner as in example 45. The results are shown in Table 7.
Examples 90 to 92 and comparative examples 53 to 55
A mineral-fortified yogurt was obtained in the same manner as in example 89, except that the inorganic particle-containing additive slurry compositions or their powder compositions prepared in examples 16, 29, and 43 and comparative examples 1, 13, and 24 were used and the total weight of the mineral content was adjusted to the same concentration as in example 89. The observation of the amount of precipitation and the sensory test of the flavor of these mineral-fortified yoghurts were carried out in the same manner as in example 45. The results are shown in Table 7.
TABLE 7
The additive slurry composition or powder composition containing inorganic particles Amount of precipitate Flavor (I) and flavor (II)
After 3 days After 7 days After 14 days
Example 89 Composition prepared according to example 2 4 3 3 4
Example 90 Composition prepared according to example 16 5 5 5 6
Example 91 Composition prepared according to example 29 4 3 2 5
Example 92 Composition prepared according to example 43 5 5 5 6
Comparative example 53 Composition prepared according to comparative example 1 4 3 2 2
Comparative example 54 Composition prepared according to comparative example 13 5 5 4 3
Comparative example 55 Composition prepared according to comparative example 24 5 5 4 3
Example 93
Extracting roasted and pulverized coffee beans, and extracting coffee liquid to obtain coffee extract. To 8kg of this coffee extract, 220g of granulated sugar, 2kg of cow milk, and the additive slurry composition containing inorganic particles prepared in example 2 were mixed so that the amount of calcium was 64g, and the mixture was stirred, and then water was added so that the total amount was 20kg, and further stirred. Then, sodium bicarbonate was added to adjust the pH to 6.7, followed by homogenization to obtain a mixed solution. Canning the flavoring liquid, and instantly sterilizing at 123 deg.C under high pressure for 20 min to obtain canned beverage containing calcium-enriched coffee.
The sensory test of the coffee canned beverage was carried out in the same manner as in example 45. The results are shown in Table 8.
Examples 94 to 102 and comparative examples 56 to 61
A mineral-fortified coffee canned beverage was obtained in the same manner as in example 93, except that the additive slurry compositions containing inorganic particles or their powder compositions prepared in examples 11, 17, 18, 21, 30, 38, 41, 42, and 44 and comparative examples 2, 11, 12, 14, 22, and 26 were used and the total weight of the mineral content was adjusted to the same concentration as in example 93. The amount of sediment and the sensory test of flavor of these mineral-fortified coffee canned beverages were carried out in the same manner as in example 45. The results are shown in Table 8.
TABLE 8
The additive slurry composition or powder composition containing inorganic particles Amount of precipitate Flavor (I) and flavor (II)
After 30 days After 60 days After 90 days
Example 93 Composition prepared according to example 2 4 3 2 4
Example 94 Composition prepared according to example 11 3 3 2 5
Example 95 Composition prepared according to example 17 5 5 4 6
Example 96 Composition prepared according to example 18 5 5 4 6
Example 97 Composition prepared according to example 21 5 5 5 6
Example 98 Composition prepared according to example 30 4 3 2 6
Example 99 Composition prepared according to example 38 5 5 4 6
Example 100 Composition prepared according to example 41 5 5 4 5
Example 101 Composition prepared according to example 42 5 5 5 6
Example 102 Composition prepared according to example 44 5 5 5 6
Comparative example 56 Composition prepared according to comparative example 2 4 3 2 1
Comparative example 57 Composition prepared according to comparative example 11 5 4 4 3
Comparative example 58 Composition prepared according to comparative example 12 5 4 4 2
Comparative example 59 Composition prepared according to comparative example 14 3 3 2 2
Comparative example 60 Composition prepared according to comparative example 22 1 1 1 3
Comparative example 61 Composition prepared according to comparative example 26 5 5 4 3
Industrial applicability
As described above, the inorganic particle-containing additive slurry composition and the powder composition thereof of the present invention are extremely excellent not only in redispersibility in a liquid and long-term storage stability in a liquid, but also in flavor, which is one of the most important aspects of food products.

Claims (11)

1. An additive composition comprising inorganic particles, the composition comprising at least one polyvalent metal selected from the group consisting of calcium, magnesium, and iron, phosphate ions, an organic acid having a carboxyl group, and at least one alkali metal selected from the group consisting of sodium and potassium, with the following conditions (a) and (b):
(a)70≤X≤90000
x: the amount (mg/kg) of alkali metal contained in the solid component of the additive composition containing inorganic particles
(b)0.1≤Y≤15
Y: the additive composition containing inorganic particles was adjusted to a conductivity (mS/cm) at a solid content concentration of 10% by weight.
2. The additive composition containing inorganic particles according to claim 1, which comprises at least one polyvalent metal selected from the group consisting of calcium, magnesium, iron, phosphate ion, organic acid having carboxyl group and at least one alkali metal selected from the group consisting of sodium and potassium, with the following conditions (c) and (d):
(c)70≤X≤39000
x: the amount (mg/kg) of alkali metal contained in the solid component of the additive composition containing inorganic particles
(d)0.1≤Y≤7
Y: the additive composition containing inorganic particles was adjusted to a conductivity (mS/cm) at a solid content concentration of 10% by weight.
3. The inorganic particle-containing additive composition according to claim 2, which comprises at least one polyvalent metal selected from the group consisting of calcium, magnesium, and iron, phosphate ions, an organic acid having a carboxyl group, and at least one alkali metal selected from the group consisting of sodium and potassium, with the following conditions (e) and (f):
(e)150≤X≤10000
x: the amount (mg/kg) of alkali metal contained in the solid component of the additive composition containing inorganic particles
(f)0.25≤Y≤1.8
Y: the additive composition containing inorganic particles was adjusted to a conductivity (mS/cm) at a solid content concentration of 10% by weight.
4. An additive composition comprising inorganic particles according to claim 1, characterized in that: the additive composition is prepared by a method selected from the following (I) to (IV), is composed of a composition containing a polyvalent metal mainly composed of at least one phosphoric acid compound selected from the group consisting of calcium phosphate, magnesium phosphate and iron phosphate, a phosphate ion, an organic acid having a carboxyl group and at least one alkali metal selected from the group consisting of sodium and potassium, and has the following conditions (a) and (b),
(I) mixing water with a polyvalent metal compound, an organic acid having a carboxyl group and an alkali metal source to prepare a precursor, adding a phosphoric acid source to the precursor,
(II) mixing water with a polyvalent metal compound, a phosphoric acid source, and an alkali metal source or a phosphoric acid source/alkali metal source to prepare a precursor, adding an organic acid having a carboxyl group to the precursor,
(III) mixing water with a polyvalent metal compound and an organic acid having a carboxyl group to prepare a precursor, adding a phosphoric acid source and an alkali metal source to the precursor,
(IV) mixing water with a polyvalent metal compound, an organic acid having a carboxyl group and a phosphoric acid source to prepare a precursor, and adding an alkali metal source to the precursor;
(a)70≤X≤90000
x: the amount (mg/kg) of alkali metal contained in the solid component of the additive composition containing inorganic particles
(b)0.1≤Y≤15
Y: the additive composition containing inorganic particles was adjusted to a conductivity (mS/cm) at a solid content concentration of 10% by weight.
5. An additive composition containing inorganic particles, which contains 2 to 80 parts by weight of an emulsion stabilizer relative to 100 parts by weight of the solid content of the additive composition containing inorganic particles of claim 1.
6. The inorganic particle-containing additive composition of any one of claims 1 to 5, wherein the weight average particle diameter K (μm) in the particle size distribution of the inorganic particle-containing additive composition is 0.02. ltoreq. K.ltoreq.0.8.
7. The inorganic particle-containing additive composition according to any one of claims 1 to 5, which is an inorganic particle-containing additive composition for food.
8. A process for the preparation of an additive composition comprising inorganic particles, characterized in that: preparing a slurry containing a polyvalent metal having at least one phosphoric acid compound selected from the group consisting of calcium, magnesium and iron as a main component, a phosphoric acid ion, an organic acid having a carboxyl group and at least one alkali metal selected from the group consisting of sodium and potassium by a method selected from the group consisting of (I) to (IV) described below, and then washing the slurry,
(I) mixing water with a polyvalent metal compound, an organic acid having a carboxyl group, and an alkali metal source to prepare a precursor material, and adding a phosphoric acid source to the precursor material;
(II) mixing water with a polyvalent metal compound, a phosphoric acid source, and an alkali metal source or a phosphoric acid source/alkali metal source to prepare a precursor, and adding an organic acid having a carboxyl group to the precursor;
(III) mixing water with a polyvalent metal compound and an organic acid having a carboxyl group to prepare a precursor, and adding a phosphoric acid source and an alkali metal source to the precursor;
(IV) mixing water with a polyvalent metal compound, an organic acid having a carboxyl group and a phosphoric acid source to prepare a precursor, and adding an alkali metal source to the precursor.
9. A process for the preparation of an additive composition comprising inorganic particles, characterized in that: the emulsion stabilizer is contained in an amount of 2 to 80 parts by weight based on 100 parts by weight of the solid content of the additive composition containing inorganic particles prepared by the method of claim 8.
10. A process for the preparation of an additive composition comprising inorganic particles according to claim 9, characterized in that: after the emulsion stabilizer is added, it is dispersed by a pulverizer and/or a disperser.
11. Food composition, characterized in that it is constituted by an additive composition containing inorganic particles according to any one of claims 1 to 5.
HK05108476.1A 2001-10-16 2002-10-15 Inorganic-particle-containing additive composition, process for producing the same, and food composition containing the additive composition HK1076358B (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP317872/2001 2001-10-16
JP2001317872 2001-10-16
PCT/JP2002/010659 WO2003032752A1 (en) 2001-10-16 2002-10-15 Inorganic-particle-containing additive composition, process for producing the same, and food composition containing the additive composition

Publications (2)

Publication Number Publication Date
HK1076358A1 HK1076358A1 (en) 2006-01-20
HK1076358B true HK1076358B (en) 2007-06-29

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