JP4625586B2 - Magnesium hydroxide granular material and granular fertilizer containing magnesium hydroxide - Google Patents
Magnesium hydroxide granular material and granular fertilizer containing magnesium hydroxide Download PDFInfo
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- JP4625586B2 JP4625586B2 JP2001028073A JP2001028073A JP4625586B2 JP 4625586 B2 JP4625586 B2 JP 4625586B2 JP 2001028073 A JP2001028073 A JP 2001028073A JP 2001028073 A JP2001028073 A JP 2001028073A JP 4625586 B2 JP4625586 B2 JP 4625586B2
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- magnesium hydroxide
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Description
【0001】
【発明の属する技術分野】
本発明は、肥料用として好適な水酸化マグネシウム粒状物に関する。
【0002】
【従来の技術】
マグネシウムは植物の五大栄養素の一つであり、葉緑素の主成分であると同時に、リン酸の吸収や植物体内での移動を促進する重要な役割を果たす。植物はマグネシウムが欠乏すると、葉面が黄色化したり、落葉したり、さらには枯死したりする。このような植物中のマグネシウムの欠乏による弊害を防止することを目的として苦土肥料(酸化マグネシウム)、水酸化苦土肥料(水酸化マグネシウム)、硫酸苦土肥料(硫酸マグネシウム)などのマグネシウム含有肥料が利用されている。マグネシウム含有肥料の中でも、水酸化苦土肥料は、アルカリ性を示すことから、酸性土壌に特に有効であって、かつ酸化マグネシウムのように保存中に大気中の水分と反応して凝結しにくいなどの利点を有しているため特に有用である。
【0003】
マグネシウム含有肥料は、従来では単独で施肥されていたが、最近では、バルクブレンド配合肥料の一成分としての利用も検討されている。バルクブレンド配合肥料は、施肥位置によって肥料組成が変化しないように、肥料全体にわたって均質性を示すことが望ましい。従って、バルクブレンド配合肥料に用いる粒状肥料は、機械的な衝撃により容易に崩壊しないように硬度が高いものが好ましいとされている。
【0004】
硬度の高い肥料用水酸化マグネシウム粒状物として、特開平11−343187号公報には、水酸化マグネシウム粉末とバインダ(硫酸マグネシウム水溶液)とを混合造粒して得た水酸化マグネシウム粒状物が提案されている。この公報の実施例では、硬度が3〜6kgの水酸化マグネシウム粒状物が得られている。
【0005】
【発明が解決しようとする課題】
硬度の高い水酸化マグネシウム粒状物は、機械的な衝撃を受けても崩壊しにくい。しかし、本発明者の研究によれば、硬度の高い水酸化マグネシウム粒状物であっても、輸送や施肥の際に、水酸化マグネシウム粒状物と水酸化マグネシウム粒状物(あるいは他の粒状肥料)とが接触することによって、水酸化マグネシウム粒状物の表面が削られて粉末状の水酸化マグネシウムが生成することがあることが明らかになった。
【0006】
水酸化マグネシウム粒状物の表面を削られにくくする(すなわち、表面の強度を高める)方法としては、水酸化マグネシウム粉末から造粒物を製造する際に加えるバインダの添加量を増やすのが有効である。しかし、本発明者の検討によれば、バインダの添加量を多くし過ぎると、水酸化マグネシウム粉末から造粒物を製造することが難しくなる傾向があり、通常の工業的な造粒装置において問題とならない程度のバインダ添加量では、水酸化マグネシウム粒状物の表面の強度を、その表面が削られにくくなるまで高めることが難しいことが判明した。
【0007】
従って、本発明の目的は、工業的に容易に生産でき、かつ輸送や施肥の際に水酸化マグネシウム粉末が生成しにくい水酸化マグネシウム粒状物を提供することにある。本発明は、また、輸送や施肥の際に水酸化マグネシウム粉末が生成しにくい水酸化マグネシウム粒状物の製造方法を提供することも、その目的とする。本発明は、さらに、水酸化マグネシウム粉末が生成しにくい水酸化マグネシウム粒状物を有効成分とする肥料を提供することも、その目的とする。
【0008】
【課題を解決するための手段】
本発明は、平均粒径が1〜5mmの範囲内にある粒状水酸化マグネシウムを核とし、その周囲に硫酸と水酸化マグネシウム粒子との反応生成物からなる被覆層が二層以上形成されていることを特徴とする水酸化マグネシウム粒状物にある。
【0009】
本発明の水酸化マグネシウム粒状物は、その表面に強度の強い被覆層が二層以上形成されているので水酸化マグネシウム粉末が生成しにくい、すわなち、下記の方法により測定される粉化率が低くなる。本発明の水酸化マグネシウム粒状物における好ましい粉化率は10%以下である。
【0010】
(1)円筒状磁性ポット(内径100mm×深さ100mm)に、水酸化マグネシウム粒状物100g、及び直径が約30mm、重量が約35gの磁性ボールを合計重量が105g程度になるように三個投入して蓋をする。
(2)円筒状磁性ポットを横に倒した状態で軸位置で毎分75回転の速さで15分間回転させる。
(3)磁性ポットから水酸化マグネシウム粒状物を取り出し、標準ふるいにより16メッシュ以下の粉化物を採取し、その重量(A)を求めて、下記式(1)により粉化率を求める。
【0011】
粉化率(%)=A(g)/100(g)×100・・・(1)
【0012】
本発明は、また、平均粒径が1〜5mmの範囲内にある粒状水酸化マグネシウム20〜60質量部、水分が2質量%未満で平均粒径が1mm未満の水酸化マグネシウム粉末5〜30質量部、水分が2〜30質量%の水酸化マグネシウムケーキ5〜30質量部、そして濃度が3〜18モル/リットルの硫酸1.5〜4.0質量部をそれぞれ混合し造粒した後、さらに水分が2質量%未満で平均粒径が1mm未満の水酸化マグネシウム粉末5〜30質量部、水分が2〜30質量%の水酸化マグネシウムケーキ5〜30質量部、そして濃度が3〜18モル/リットルの硫酸1.5〜4.0質量部を加えて造粒し、乾燥することを含む水酸化マグネシウム粒状物の製造方法にもある。
【0013】
本発明は、さらに、前記の水酸化マグネシウム粒状物を有効成分として含む水酸化マグネシウム含有粒状肥料(バルクブレンド配合肥料)にもある。
【0014】
【発明の実施の形態】
本発明の水酸化マグネシウム粒状物は、粒状水酸化マグネシウムを核とし、その周囲に硫酸と水酸化マグネシウム粒子との反応生成物からなる被覆層が二層以上形成されていることを特徴としている。すなわち、本発明の水酸化マグネシウム粒状物は、二層以上の被覆層で覆われていることを特徴としている。本発明の水酸化マグネシウム粒状物において、被覆層は、通常は、二〜四層の範囲内、好ましくは二層である。
【0015】
本発明の水酸化マグネシウム粒状物において核となる粒状水酸化マグネシウムは、平均粒径が1〜5mmの範囲内、好ましくは2〜3mmの範囲内にある球形であることが望ましい。粒状水酸化マグネシウムの製造方法に特には制限はない。例えば、水酸化マグネシウム粉末とバインダ(通常は、硫酸)とをヘンシェルミキサなどの撹拌造粒機に投入し、撹拌混合して造粒することにより製造することができる。
【0016】
本発明において、被覆層は、硫酸と水酸化マグネシウム粒子との反応生成物からなる。硫酸と水酸化マグネシウム粒子との反応生成物には、硫酸マグネシウム水溶液と水酸化マグネシウム粒子との反応生成物も含まれる。被覆層は、硫酸源及び水酸化マグネシウム粒子源を粒状水酸化マグネシウム(核)とともに撹拌混合して造粒することにより形成することができる。撹拌混合には、ヘンシェルミキサなどの通常の撹拌造粒機を用いることができる。
【0017】
被覆層の硫酸源には、硫酸あるいは硫酸マグネシウム水溶液を用いることができる。通常は、濃度が3〜18モル/リットル(好ましくは8〜13モル/リットル)の範囲内にある硫酸を用いる。
【0018】
硫酸源の添加量は、被覆層に含まれる硫酸成分(硫酸イオン量)が6〜15質量%の範囲内になる量であることが好ましい。被覆層に含まれる硫酸成分の量が6質量%未満であると、被覆層の強度が低くなる。一方、硫酸源の添加量を多くし過ぎると造粒しにくくなる。
【0019】
被覆層の水酸化マグネシウム粒子源には、水分が2質量%未満の水酸化マグネシウム粉末、あるいは水分が2〜30質量%の水酸化マグネシウムケーキ、もしくはこれらを併用して用いることができる。通常は、水酸化マグネシウム粉末と水酸化マグネシウムケーキの混合物を用いる。
【0020】
水酸化マグネシウム粒子源として用いる水酸化マグネシウム粉末は、平均粒径が1mm以下、好ましくは100μm以下である。水酸化マグネシウム粉末には、材料コストの観点から、核となる粒状水酸化マグネシウムの製造の際に得られる核として使用するには適さない大きさの粒状水酸化マグネシウムを粉砕して粉末としたものを用いることが好ましい。
【0021】
水酸化マグネシウム粒子源として用いる水酸化マグネシウムケーキの大きさや形状には特別な制限はない。水酸化マグネシウムケーキには、海水に石灰乳を加えて得た水酸化マグネシウムスラリーを濃縮脱水して得たものを用いることができる。
【0022】
本発明の水酸化マグネシウム粒状物は、単独であるいは他の粒状肥料と混合して肥料として用いることができる。他の粒状肥料には、硫酸アンモニウム肥料、硝酸アンモニウム肥料、塩化アンモニウム肥料、硝酸石灰肥料、石灰窒素肥料、リン酸塩肥料、尿素肥料、消石灰肥料、及び炭酸カルシウム肥料などを用いることができる。
【0023】
【実施例】
[実施例1]
(1)粒状水酸化マグネシウム(核)の製造
粒径が0.1〜0.5mmの範囲内にある水酸化マグネシウム粉末85質量部と濃度が11.5モル/リットルの硫酸15質量部をヘンシェルミキサに投入し、撹拌混合して造粒して粒状水酸化マグネシウム(硫酸成分量10質量%)を得た。得られた粒状水酸化マグネシウムを120℃で乾燥して水分を1重量%以下とした後、篩分けし、粒径が2〜3mmの粒状水酸化マグネシウムを選別してこれを核とした。なお、粒径が2〜3mm以外の大きさの粒状水酸化マグネシウムは、粉砕機で粒径が100μm以下になるまで粉砕して、被覆層の水酸化マグネシウム源として用いた。
【0024】
(2)一層目の被覆層の形成
粒径が2〜3mmの範囲内にある粒状水酸化マグネシウム25質量部、粒径が100μm以下の水酸化マグネシウム粉末(水分1質量%、硫酸成分量10質量%)10質量部、水酸化マグネシウムケーキ(水分22質量%)15質量部及び濃度が11.5モル/リットルの硫酸1.88質量部をそれぞれヘンシェルミキサに投入し、混合撹拌して造粒した。
【0025】
(3)二層目の被覆層の形成
続いて、上記のヘンシェルミキサに、粒径が100μm以下の水酸化マグネシウム粉末(水分1質量%、硫酸成分量10質量%)25質量部、水酸化マグネシウムケーキ(水分22質量%)25質量部及び濃度が11.5モル/リットルの硫酸3.12質量部を投入し、混合撹拌して造粒して、二層目の被覆層を形成した。次いで、得られた粒状物を120℃で乾燥した。乾燥後の粒状物は粒径が2.8〜4.0mmであった。
【0026】
[評価及び結果]
(1)実施例1で製造した水酸化マグネシウム粒状物の断面を顕微鏡で観察した。その顕微鏡写真を図1に示す。図1に示すように、実施例1で製造した水酸化マグネシウム粒状物は、粒状水酸化マグネシウムを核として、その周囲に二層の被覆層が形成されていることがわかる。
【0027】
(2)実施例1で製造した水酸化マグネシウム粒状物の粉化率を前記の方法により測定したところ、7.6%であった。
【0028】
【発明の効果】
本発明の水酸化マグネシウム粒状物は、表面が二層以上の被覆層で覆われているので強度が強く、輸送や施肥の際にその表面の削れによる粉末状の水酸化マグネシウムが生成しにくい。従って、本発明の水酸化マグネシウム粒状物を有効成分として含む水酸化マグネシウム含有粒状肥料(バルクブレンド配合肥料)は均質性が高い。
本発明の水酸化マグネシウム粒状物の製造方法によれば、輸送や施肥の際に粉末状の水酸化マグネシウムが発生しにくい水酸化マグネシウム粒状物を工業的に容易に製造することができる。
【図面の簡単な説明】
【図1】実施例1にて製造した水酸化マグネシウム粒状物の断面写真である。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a magnesium hydroxide granular material suitable for use as a fertilizer.
[0002]
[Prior art]
Magnesium is one of the five major nutrients of plants and is the main component of chlorophyll, and at the same time plays an important role in promoting phosphate absorption and movement within the plant. When a plant is deficient in magnesium, the leaves become yellow, fallen leaves, and even die. Magnesium-containing fertilizers such as bitter fertilizer (magnesium oxide), hydroxylated bitter fertilizer (magnesium hydroxide), and sulfated bitter fertilizer (magnesium sulfate) for the purpose of preventing the harmful effects of magnesium deficiency in plants. Is being used. Among magnesium-containing fertilizers, hydroxylated mashed fertilizers are alkaline, and are particularly effective in acidic soils, and are unlikely to condense by reacting with atmospheric moisture during storage, such as magnesium oxide. It is particularly useful because it has advantages.
[0003]
Magnesium-containing fertilizers have conventionally been applied alone, but recently, use as a component of bulk blended fertilizers has also been studied. It is desirable for the bulk blend compound fertilizer to show homogeneity throughout the fertilizer so that the fertilizer composition does not change depending on the fertilization position. Therefore, the granular fertilizer used for the bulk blended fertilizer is preferably high in hardness so as not to easily disintegrate due to mechanical impact.
[0004]
As a magnesium hydroxide granule for fertilizer having high hardness, JP-A-11-343187 proposes a magnesium hydroxide granule obtained by mixing and granulating magnesium hydroxide powder and a binder (magnesium sulfate aqueous solution). Yes. In the examples of this publication, granular magnesium hydroxide having a hardness of 3 to 6 kg is obtained.
[0005]
[Problems to be solved by the invention]
The magnesium hydroxide granular material having high hardness is not easily broken even when subjected to mechanical impact. However, according to the inventor's study, magnesium hydroxide granules and magnesium hydroxide granules (or other granular fertilizers) can be used during transportation and fertilization even if the magnesium hydroxide granules have high hardness. It has been clarified that the surface of the magnesium hydroxide granular material may be scraped to produce powdered magnesium hydroxide.
[0006]
As a method of making the surface of the magnesium hydroxide granular material difficult to be scraped (that is, increasing the strength of the surface), it is effective to increase the amount of binder added when producing the granulated material from the magnesium hydroxide powder. . However, according to the study of the present inventor, if the amount of binder added is excessively large, it tends to be difficult to produce a granulated product from magnesium hydroxide powder, which is a problem in ordinary industrial granulating equipment. It has been found that it is difficult to increase the strength of the surface of the magnesium hydroxide granular material until the surface becomes difficult to be scraped with a binder addition amount that does not become so.
[0007]
Accordingly, an object of the present invention is to provide a magnesium hydroxide granular material that can be easily produced industrially and is difficult to produce magnesium hydroxide powder during transportation and fertilization. Another object of the present invention is to provide a method for producing a magnesium hydroxide granular material in which magnesium hydroxide powder is less likely to be produced during transportation and fertilization. Another object of the present invention is to provide a fertilizer containing magnesium hydroxide granular material that is difficult to produce magnesium hydroxide powder as an active ingredient.
[0008]
[Means for Solving the Problems]
In the present invention, granular magnesium hydroxide having an average particle diameter in the range of 1 to 5 mm is used as a core, and two or more coating layers made of a reaction product of sulfuric acid and magnesium hydroxide particles are formed around the magnesium hydroxide. It is in the magnesium hydroxide granular material characterized by this.
[0009]
The magnesium hydroxide granular material of the present invention has two or more strong coating layers formed on the surface thereof, so that it is difficult to produce magnesium hydroxide powder. In other words, the powdering rate measured by the following method Becomes lower. The preferable powdering rate in the magnesium hydroxide granular material of the present invention is 10% or less.
[0010]
(1) Three cylindrical magnetic pots (inner diameter: 100 mm × depth: 100 mm) with 100 g of magnesium hydroxide particles and magnetic balls with a diameter of about 30 mm and a weight of about 35 g are added so that the total weight is about 105 g. And cover.
(2) Rotate the cylindrical magnetic pot for 15 minutes at a speed of 75 revolutions per minute at the axial position in a state where the cylindrical magnetic pot is tilted sideways.
(3) Magnesium hydroxide particulates are taken out from the magnetic pot, and a powder of 16 mesh or less is collected with a standard sieve, its weight (A) is obtained, and the powdering rate is obtained by the following formula (1).
[0011]
Powdering rate (%) = A (g) / 100 (g) × 100 (1)
[0012]
The present invention also includes 20 to 60 parts by mass of granular magnesium hydroxide having an average particle size in the range of 1 to 5 mm, 5 to 30 masses of magnesium hydroxide powder having a water content of less than 2% by mass and an average particle size of less than 1 mm. 1 part by weight, 5 to 30 parts by weight of magnesium hydroxide cake having a moisture content of 2 to 30% by weight, and 1.5 to 4.0 parts by weight of sulfuric acid having a concentration of 3 to 18 mol / liter, respectively, 5-30 parts by mass of magnesium hydroxide powder having a moisture content of less than 2% by mass and an average particle size of less than 1 mm, 5-30 parts by mass of magnesium hydroxide cake having a moisture content of 2-30% by mass, and a concentration of 3-18 mol / There is also a method for producing a magnesium hydroxide granular material, which includes adding 1.5 to 4.0 parts by mass of liter of sulfuric acid, granulating and drying.
[0013]
The present invention also resides in a magnesium hydroxide-containing granular fertilizer (bulk blend compound fertilizer) containing the magnesium hydroxide granular material as an active ingredient.
[0014]
DETAILED DESCRIPTION OF THE INVENTION
The magnesium hydroxide granular material of the present invention is characterized in that two or more coating layers made of a reaction product of sulfuric acid and magnesium hydroxide particles are formed around granular magnesium hydroxide. That is, the magnesium hydroxide granular material of the present invention is characterized by being covered with two or more coating layers. In the magnesium hydroxide granular material of the present invention, the coating layer is usually in the range of 2 to 4 layers, preferably 2 layers.
[0015]
The granular magnesium hydroxide as a nucleus in the magnesium hydroxide granular material of the present invention desirably has a spherical shape with an average particle diameter in the range of 1 to 5 mm, preferably in the range of 2 to 3 mm. There is no restriction | limiting in particular in the manufacturing method of granular magnesium hydroxide. For example, magnesium hydroxide powder and a binder (usually sulfuric acid) are put into an agitation granulator such as a Henschel mixer, and the mixture can be agitated and mixed for granulation.
[0016]
In the present invention, the coating layer is made of a reaction product of sulfuric acid and magnesium hydroxide particles. The reaction product of sulfuric acid and magnesium hydroxide particles also includes a reaction product of magnesium sulfate aqueous solution and magnesium hydroxide particles. The coating layer can be formed by stirring and mixing a sulfuric acid source and a magnesium hydroxide particle source together with granular magnesium hydroxide (core) and granulating. For stirring and mixing, a normal stirring granulator such as a Henschel mixer can be used.
[0017]
As the sulfuric acid source of the coating layer, sulfuric acid or a magnesium sulfate aqueous solution can be used. Usually, sulfuric acid having a concentration of 3 to 18 mol / liter (preferably 8 to 13 mol / liter) is used.
[0018]
The addition amount of the sulfuric acid source is preferably an amount such that the sulfuric acid component (sulfuric acid ion amount) contained in the coating layer falls within the range of 6 to 15% by mass. The intensity | strength of a coating layer becomes it low that the quantity of the sulfuric acid component contained in a coating layer is less than 6 mass%. On the other hand, if the amount of the sulfuric acid source added is too large, granulation becomes difficult.
[0019]
As the magnesium hydroxide particle source of the coating layer, a magnesium hydroxide powder having a moisture content of less than 2% by mass, a magnesium hydroxide cake having a moisture content of 2 to 30% by mass, or a combination thereof can be used. Usually, a mixture of magnesium hydroxide powder and magnesium hydroxide cake is used.
[0020]
The magnesium hydroxide powder used as the magnesium hydroxide particle source has an average particle size of 1 mm or less, preferably 100 μm or less. Magnesium hydroxide powder is obtained by pulverizing granular magnesium hydroxide of a size unsuitable for use as a core obtained in the production of the core magnesium hydroxide from the viewpoint of material cost. Is preferably used.
[0021]
There is no particular limitation on the size and shape of the magnesium hydroxide cake used as the magnesium hydroxide particle source. As the magnesium hydroxide cake, a cake obtained by concentrating and dehydrating a magnesium hydroxide slurry obtained by adding lime milk to seawater can be used.
[0022]
The magnesium hydroxide granular material of the present invention can be used as a fertilizer alone or mixed with other granular fertilizers. Examples of other granular fertilizers include ammonium sulfate fertilizer, ammonium nitrate fertilizer, ammonium chloride fertilizer, lime nitrate fertilizer, lime nitrogen fertilizer, phosphate fertilizer, urea fertilizer, slaked lime fertilizer, and calcium carbonate fertilizer.
[0023]
【Example】
[Example 1]
(1) Production of granular magnesium hydroxide (core) 85 parts by mass of magnesium hydroxide powder in the range of 0.1 to 0.5 mm and 15 parts by mass of sulfuric acid having a concentration of 11.5 mol / liter The mixture was put into a mixer, mixed with stirring and granulated to obtain granular magnesium hydroxide (sulfuric acid component amount: 10% by mass). The obtained granular magnesium hydroxide was dried at 120 ° C. to reduce the water content to 1% by weight or less, and sieved to select granular magnesium hydroxide having a particle size of 2 to 3 mm, which was used as a core. The granular magnesium hydroxide having a particle size other than 2 to 3 mm was pulverized with a pulverizer until the particle size became 100 μm or less, and used as a magnesium hydroxide source for the coating layer.
[0024]
(2) 25 parts by mass of granular magnesium hydroxide having a coating particle size of the first coating layer in the range of 2 to 3 mm, magnesium hydroxide powder having a particle size of 100 μm or less (water 1 mass%, sulfuric acid component content 10 mass) %) 10 parts by weight, 15 parts by weight of magnesium hydroxide cake (water content 22% by weight) and 1.88 parts by weight of sulfuric acid having a concentration of 11.5 mol / liter were each put into a Henschel mixer, mixed and stirred for granulation. .
[0025]
(3) Formation of second coating layer Subsequently, 25 parts by mass of magnesium hydroxide powder having a particle size of 100 μm or less (water content 1 mass%, sulfuric acid component content 10 mass%), magnesium hydroxide 25 parts by mass of cake (water content 22% by mass) and 3.12 parts by mass of sulfuric acid having a concentration of 11.5 mol / liter were added, mixed and stirred, and granulated to form a second coating layer. The resulting granulate was then dried at 120 ° C. The granular material after drying had a particle size of 2.8 to 4.0 mm.
[0026]
[Evaluation and results]
(1) The cross section of the magnesium hydroxide granular material produced in Example 1 was observed with a microscope. The micrograph is shown in FIG. As shown in FIG. 1, it can be seen that the magnesium hydroxide granular material produced in Example 1 has two layers of coating layers formed around the granular magnesium hydroxide as a core.
[0027]
(2) When the powdering rate of the magnesium hydroxide granular material manufactured in Example 1 was measured by the above method, it was 7.6%.
[0028]
【The invention's effect】
The magnesium hydroxide granular material of the present invention has a high strength because the surface is covered with two or more coating layers, and powder magnesium hydroxide is hardly generated due to scraping of the surface during transportation or fertilization. Therefore, the magnesium hydroxide containing granular fertilizer (bulk blend compound fertilizer) which contains the magnesium hydroxide granular material of this invention as an active ingredient has high homogeneity.
According to the manufacturing method of the magnesium hydroxide granular material of the present invention, the magnesium hydroxide granular material that hardly generates powdered magnesium hydroxide during transportation and fertilization can be easily industrially manufactured.
[Brief description of the drawings]
1 is a cross-sectional photograph of a magnesium hydroxide granular material produced in Example 1. FIG.
Claims (4)
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KR100767733B1 (en) | 2006-05-18 | 2007-10-17 | 주식회사 포스렉 | Composite fertilizer with mineral elements and method for producing the composite fertilizer |
JP2008247653A (en) * | 2007-03-29 | 2008-10-16 | Sumitomo Chemical Co Ltd | Method of manufacturing granular fertilizer composition and granular fertilizer composition |
CN109923093B (en) * | 2017-02-24 | 2020-12-25 | 株式会社宫本制作所 | Fertilizer for plant cultivation comprising washing wastewater, method for plant cultivation using same, and method for using washing wastewater as fertilizer for plant cultivation |
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Citations (9)
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JPS63277510A (en) * | 1987-05-11 | 1988-11-15 | Shin Nippon Kagaku Kogyo Co Ltd | Production of magnesium hydroxide and surface-treated magnesium hydroxide |
JPH02289421A (en) * | 1989-04-27 | 1990-11-29 | Ube Chem Ind Co Ltd | Magnesium hydroxide particle |
JPH02289420A (en) * | 1989-04-27 | 1990-11-29 | Ube Chem Ind Co Ltd | Magnesium hydroxide particle |
JPH02293317A (en) * | 1989-05-01 | 1990-12-04 | Ube Chem Ind Co Ltd | Magnesium hydroxide particle |
JPH02293316A (en) * | 1989-05-01 | 1990-12-04 | Ube Ind Ltd | Magnesium hydroxide particle |
JPH03131516A (en) * | 1989-10-17 | 1991-06-05 | Asahi Glass Co Ltd | Granular magnesium hydroxide and production thereof |
JPH03170324A (en) * | 1989-11-27 | 1991-07-23 | Mitsubishi Materials Corp | Surface treatment of magnesium hydroxide |
JPH11343187A (en) * | 1998-06-01 | 1999-12-14 | Tosoh Corp | Granular magnesium hydroxide fertilizer and its production |
JP2001233687A (en) * | 2000-02-22 | 2001-08-28 | Ube Material Industries Ltd | Magnesium hydroxide granule for fertilizer |
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Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63277510A (en) * | 1987-05-11 | 1988-11-15 | Shin Nippon Kagaku Kogyo Co Ltd | Production of magnesium hydroxide and surface-treated magnesium hydroxide |
JPH02289421A (en) * | 1989-04-27 | 1990-11-29 | Ube Chem Ind Co Ltd | Magnesium hydroxide particle |
JPH02289420A (en) * | 1989-04-27 | 1990-11-29 | Ube Chem Ind Co Ltd | Magnesium hydroxide particle |
JPH02293317A (en) * | 1989-05-01 | 1990-12-04 | Ube Chem Ind Co Ltd | Magnesium hydroxide particle |
JPH02293316A (en) * | 1989-05-01 | 1990-12-04 | Ube Ind Ltd | Magnesium hydroxide particle |
JPH03131516A (en) * | 1989-10-17 | 1991-06-05 | Asahi Glass Co Ltd | Granular magnesium hydroxide and production thereof |
JPH03170324A (en) * | 1989-11-27 | 1991-07-23 | Mitsubishi Materials Corp | Surface treatment of magnesium hydroxide |
JPH11343187A (en) * | 1998-06-01 | 1999-12-14 | Tosoh Corp | Granular magnesium hydroxide fertilizer and its production |
JP2001233687A (en) * | 2000-02-22 | 2001-08-28 | Ube Material Industries Ltd | Magnesium hydroxide granule for fertilizer |
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