JPH021799B2 - - Google Patents
Info
- Publication number
- JPH021799B2 JPH021799B2 JP56159715A JP15971581A JPH021799B2 JP H021799 B2 JPH021799 B2 JP H021799B2 JP 56159715 A JP56159715 A JP 56159715A JP 15971581 A JP15971581 A JP 15971581A JP H021799 B2 JPH021799 B2 JP H021799B2
- Authority
- JP
- Japan
- Prior art keywords
- fertilizer
- white clay
- clay
- waste
- fertilizers
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- Fertilizers (AREA)
Description
本発明は固結防止された肥料組成物にかんす
る。
従来から、一般に窒素質肥料、リン酸質肥料、
カリ質肥料等の単独若しくは複合肥料が知られて
いる。そしてこれらの肥料は粉状または粒状とし
て計量あるいは使用し易い形態により市場に流通
している。
しかし乍ら、これらの肥料は、その製造工程、
特に製品移送工程、造粒工程及び製品貯蔵工程等
において、その自由流動性を失い固結する傾向が
認められる。この固結する傾向には、いくつかの
原因があり、その二つは、特に粒状複合肥料の場
合には、粒子間に微量の水分が作用するため、外
気が遮断された包装袋内であつても外温が上下す
ることにより、粒子間塩類の溶解度が変化して、
表面の溶解及び再結晶等が生じ固結する結果流動
性が失われることとなる。また、その他の原因と
しては、化学変化によるものであり、たとえば、
過リン酸石灰中の石膏が硫酸アンモニウムと反応
して複塩を生成する等の化学反応によるものであ
る。
固結防止の方法としては、肥料成分中の水分を
できるだけ少くすること、袋詰めの時にできるだ
け低温で行うこと、また、たとえば、粒状肥料に
あつてはできるだけ真球に近い粒子に成形すると
ともにできるだけ同一粒径に整粒することが挙げ
られる。また界面活性剤、珪藻土、タルク、カオ
リン、鉱滓等を使用して肥料の固結防止を行う方
法も知られている。
本発明者は、容易に、しかも従来の肥料製造工
程内において肥料の固結を防止するような方法あ
るいは添加剤を検討し本発明を完成した。
すなわち、本発明は、肥料成分に下記廃白土を
添加してなる固結防止された肥料組成物を骨子と
するものである。
廃白土:植物油脂の脱色処理に使用して脱色能
が減退した活性白土を熱処理して得られる廃
白土
植物油脂の脱色処理に使用する活性白土とし
は、モンモリロナイト、ハロサイト、を挙げるこ
とができる。
本発明に使用する廃白土としては、上記活性炭
を植物油脂の脱色に使用し脱色能が減退したもの
を、100〜400℃の温度下に間接的に加熱して得ら
れる廃白土であつて灰白色ないし黒色を呈し、か
つさらさらした粉状のものを挙げることができ
る。
加熱時間としては、30〜90分程度であり、廃白
土が充分に流動性を有する状態となればよい。
廃白土の添加量としては肥料成分に対し1〜10
重量%、好ましくは3〜5重量%程度である。こ
の量は特に特定されるものではなく、対象となる
肥料により、また肥料の形態、たとえば粉末状、
粒状等により変化するものであり、また添加量と
しても、多ければ多いだけ効果を発揮するが、少
なければそれなりに効果が期待できないものであ
る。
廃白土の添加は、肥料製造工程中いずれの工程
で添加してもよいが、できれば粉体混合工程、あ
るいは造粒工程等において添加し、充分混合する
ことが望ましい。
本発明により廃白土を添加された肥料組成物
は、充分な流動性を有し長期間固結しないもので
ある。また、廃白土を製造工程で添加された複合
肥料、たとえば魚粉等の有機質肥料、アルデヒド
加工尿素等が添加されたものは、その製造工程に
おいて、たとえば造粒工程、乾燥工程等で湿潤時
に加熱されることによつて悪臭を発生するが、本
発明の廃白土を添加することによつて、該悪臭発
生を著しく防止する等の効果のあることが判明し
た。
以下に実施例により本発明を説明するが、本発
明は以下の実施例に限定されるものではない。
実施例1〜2および比較例1〜2
(a) 造粒操作
硫酸アンモニウム、尿素、塩化カリウムおよび
消石灰を、M−2型奈良式粉砕機により1mm目ス
クーン通過まで粉砕した後、内径30cm、高さ8cm
の小型ロツシユ造粒機に仕込み、回転数35rpmに
て該造粒機を回転しながら、さらに70重量%の稀
硫酸を噴霧し、5分後さらにアンモニア水
(NH3として10重量%を含む)200gを噴霧添加
し、30分間回転を継続した。得られた造粒物をタ
バイ株式会社製パーフエクトオーブン熱風乾燥機
により75℃で10時間乾燥し、篩別して5〜12メツ
シユの範囲の粒子のものを製造した。次いで得ら
れた乾燥物を上記ロツシエ造粒機に再び仕込み、
同様に回転させつつ、ケイソウ土、石膏または本
発明の廃白土を第1表に示した量を添加し、さら
に10分間回転した。
The present invention relates to anti-caking fertilizer compositions. Conventionally, nitrogen fertilizers, phosphoric acid fertilizers,
Single or compound fertilizers such as potassium fertilizers are known. These fertilizers are distributed on the market in powdered or granular forms that are easy to measure or use. However, the manufacturing process of these fertilizers,
Particularly in the product transfer process, granulation process, product storage process, etc., there is a tendency for the product to lose its free-flowing properties and solidify. There are several reasons for this tendency to clump, and two of them are that, especially in the case of granular compound fertilizers, a small amount of moisture acts between the particles, which causes them to clump inside a packaging bag that is blocked from outside air. However, as the external temperature rises and falls, the solubility of interparticle salts changes,
As a result of surface dissolution and recrystallization and solidification, fluidity is lost. Other causes include chemical changes, such as:
This is due to a chemical reaction in which gypsum in superphosphate lime reacts with ammonium sulfate to form a double salt. Methods to prevent caking include reducing the moisture content in the fertilizer ingredients as much as possible, packing at the lowest temperature possible during bagging, and, for example, in the case of granular fertilizers, shaping the particles into particles that are as close to perfect spheres as possible. An example of this is sizing to the same particle size. Also known are methods of preventing fertilizer from caking using surfactants, diatomaceous earth, talc, kaolin, slag, and the like. The present inventor investigated a method or an additive that can easily prevent caking of fertilizer within the conventional fertilizer manufacturing process, and completed the present invention. That is, the present invention is based on a fertilizer composition that is prevented from caking and is made by adding the following waste clay to the fertilizer ingredients. Waste white clay: waste white clay obtained by heat-treating activated clay whose decolorizing ability has decreased after being used for decolorizing vegetable oils and fats Examples of activated clays used for decolorizing vegetable oils include montmorillonite and hallosite. . The waste clay used in the present invention is gray-white waste clay obtained by indirectly heating activated carbon, which has been used to decolorize vegetable oils and whose decolorizing ability has decreased, to a temperature of 100 to 400°C. Examples include smooth powders that are black or black in color. The heating time is approximately 30 to 90 minutes, as long as the waste clay becomes sufficiently fluid. The amount of waste white soil added is 1 to 10 per fertilizer component.
It is about 3% to 5% by weight, preferably about 3% to 5% by weight. This amount is not particularly specified and depends on the fertilizer in question and the form of the fertilizer, such as powdered,
It changes depending on the grain shape, etc., and the more the amount added, the more effective it will be, but if it is less, no effect can be expected. The waste clay may be added at any step during the fertilizer manufacturing process, but it is desirable to add it during the powder mixing step, granulation step, etc., and mix thoroughly. The fertilizer composition to which waste clay is added according to the present invention has sufficient fluidity and does not solidify for a long period of time. In addition, composite fertilizers made from waste white clay added during the manufacturing process, such as organic fertilizers such as fish meal, and aldehyde-processed urea, are heated during the wet process during the granulation process, drying process, etc. However, it has been found that the addition of the waste white clay of the present invention has the effect of significantly preventing the occurrence of such a bad odor. The present invention will be explained below with reference to examples, but the present invention is not limited to the following examples. Examples 1 to 2 and Comparative Examples 1 to 2 (a) Granulation operation After pulverizing ammonium sulfate, urea, potassium chloride, and slaked lime with an M-2 type Nara type pulverizer until it passes through the 1 mm screen, the powder was granulated with an inner diameter of 30 cm and a height of 30 cm. 8cm
While rotating the granulator at a rotation speed of 35 rpm, 70% by weight dilute sulfuric acid was further sprayed, and after 5 minutes, aqueous ammonia (containing 10% by weight as NH 3 ) was added. 200 g was added by spraying and rotation continued for 30 minutes. The obtained granules were dried at 75° C. for 10 hours using a Perfect Oven Hot Air Dryer manufactured by Tabai Co., Ltd., and sieved to produce particles having a size ranging from 5 to 12 meshes. Next, the obtained dried product was charged again into the above-mentioned Rossier granulator,
While rotating in the same manner, diatomaceous earth, gypsum, or the waste white clay of the present invention was added in the amount shown in Table 1, and the mixture was further rotated for 10 minutes.
【表】
(b) 強制固結試験
上記(a)項で得られた粒状肥料75gを、内径5mm
の円筒に仕込み、上方より20Kgの荷重を掛けて円
筒状のテストピースを作成した。ただし、該荷重
は、実施例1、および比較例1においては、15℃
で7日間、そして、実施例2および比較例2にお
いては45℃で2日間行つた。
上記で得られたテストピースを、丸東製作所製
の電動式一軸圧縮試験装置を使用し一軸圧縮強度
(破砕強度、ダイヤルゲージ目盛Kg/cm2)を測定
することにより強制固結試験を行つた。
第2表に示した一軸圧縮による強制固結試験
は、繰返し5回行つたものの平均値である。[Table] (b) Forced consolidation test 75g of the granular fertilizer obtained in (a) above was
A cylindrical test piece was created by placing it in a cylinder and applying a load of 20 kg from above. However, in Example 1 and Comparative Example 1, the load was 15°C.
In Example 2 and Comparative Example 2, the test was carried out at 45° C. for 2 days. A forced consolidation test was conducted on the test piece obtained above by measuring the uniaxial compression strength (crushing strength, dial gauge scale Kg/cm 2 ) using an electric uniaxial compression testing device manufactured by Maruto Seisakusho. . The forced consolidation test by uniaxial compression shown in Table 2 is the average value of 5 repeated tests.
【表】
註:固結しないためテストピースを作成す
ることができなかつた。
上記第2表から明らかなように実施例1で得ら
れた造粒物がさらさらの状態を示し、固結試験用
のテストピースを作成することが不可能であつ
た。さらに実施例2においても比較例およびコン
トロールに比較し、一軸圧縮強度が著しく小さい
ものであつた。すなわち、本発明による粒状複合
肥料は固結を生じないかたとえ固結状態を生じて
も容易に崩解しもとの流動性をとりもどすことが
明らかである。
実施例3〜8及び比較例3〜4
第3表に示す組成の原料を実施例1の造粒操作
と同様にして硝酸アンモニウム配合の粒状複合肥
料を製造した。但し本例は水造粒であり、水量は
原料の約1割を使用した。次いで実施例1(b)の強
制固結試験を行ない結果(5回繰返し)を第2表
に示した。廃白土の添加量を変化させて造粒操作
を行つたものについての結果も合せて第3表に示
した。廃白土を添加したものはいずれも破砕強度
が小さく本発明の効果の著しいことを示してい
る。[Table] Note: It was not possible to create a test piece because it did not solidify.
As is clear from Table 2 above, the granules obtained in Example 1 were in a free flowing state, making it impossible to prepare test pieces for the consolidation test. Furthermore, the unconfined compressive strength of Example 2 was also significantly lower than that of the comparative example and the control. That is, it is clear that the granular composite fertilizer according to the present invention does not cause caking, or even if it does caking, it easily disintegrates and regains its original fluidity. Examples 3 to 8 and Comparative Examples 3 to 4 Granular composite fertilizers containing ammonium nitrate were produced using raw materials having the compositions shown in Table 3 in the same manner as in the granulation procedure of Example 1. However, in this example, water granulation was used, and the amount of water used was about 10% of the raw materials. Next, the forced consolidation test of Example 1(b) was conducted and the results (repeated 5 times) are shown in Table 2. Table 3 also shows the results of granulation operations in which the amount of waste clay added was varied. All of the samples to which waste clay was added had low crushing strength, indicating that the effects of the present invention are significant.
【表】
註2:実施例1と同様にして得られたもの
実施例9〜10及び比較例5〜6
本発明により、廃白土を添加した粉状複合肥料
(第4表)の流動性について試験を行つた。
(c) 試料の作成
第4表に示した原料を配合し、実施例1で使用
した奈良式粉砕機により1mmのスクリーンを通過
するまで粉砕を行つた。[Table] Note 2: Examples 9 to 10 obtained in the same manner as Example 1 and Comparative Examples 5 to 6 Regarding the fluidity of the powdered composite fertilizer (Table 4) to which waste white clay was added according to the present invention I conducted a test. (c) Preparation of sample The raw materials shown in Table 4 were blended and ground using the Nara type grinder used in Example 1 until the material passed through a 1 mm screen.
【表】
註1:実施例1と同様にして得られたもの
(d) 流動性試験
底面の直径が120mmであり、上面の直径が15mm
であり、底面と側面とで作られる角が60゜であり、
上面が開口されている容器に、上記(c)で得られた
粉状肥料(実施例9及び比較例5)の750mlを入
れ、容器をさかさまにし、容器から落下する該肥
料の安息角及び流出時間を測定した。結果を第5
表に示す。実施例9で得られた肥料は安息角も小
さく、流出時間も速く充分に流動性のあるもので
あつた。[Table] Note 1: Obtained in the same manner as Example 1
(d) Flow test The bottom diameter is 120mm and the top diameter is 15mm.
, the angle formed by the bottom and sides is 60°,
Pour 750 ml of the powdered fertilizer obtained in (c) above (Example 9 and Comparative Example 5) into a container with an open top, turn the container upside down, and measure the angle of repose of the fertilizer falling from the container. The outflow time was measured. 5th result
Shown in the table. The fertilizer obtained in Example 9 had a small angle of repose, a fast runoff time, and sufficient fluidity.
【表】
参考例 1
本発明により廃白土を添加した肥料は、その製
造工程等において悪臭の発生を防止する作用のあ
ることを示す次の実験を行つた。
実施例9〜10及び比較例5〜6で得られれた未
乾燥造粒肥料の各200gを、1のガラスビーカ
ーに採り、ポリエチレンフイルムで覆い、100℃
の乾燥器内で1時間保持し、該ポリエチレンフイ
ルムに小孔(直径約5mm)を開け臭気について嗅
覚テストを行つた。
パネルは実験室研究員5名で構成され、次の判
定基準により行つた。結果を第6表に示す。第6
表に示した結果は5名のパネル員によつて得られ
た採点を平均したものである。[Table] Reference Example 1 The following experiment was conducted to demonstrate that the fertilizer to which waste white clay was added according to the present invention has the effect of preventing the generation of bad odors during its manufacturing process. 200g of each of the undried granulated fertilizers obtained in Examples 9-10 and Comparative Examples 5-6 was placed in a glass beaker, covered with a polyethylene film, and heated at 100°C.
The polyethylene film was kept in a dryer for 1 hour, and a small hole (about 5 mm in diameter) was made in the polyethylene film to conduct an odor test for odor. The panel consisted of five laboratory researchers, and the following criteria were used. The results are shown in Table 6. 6th
The results shown in the table are the average of the scores obtained by five panel members.
【表】 採 点 表 0点:無臭 1点:わずか 2点:やや 3点:明らかに 4点:強く 5点:耐え難い。【table】 Scoring table 0 points: odorless 1 point: slight 2 points: Somewhat 3 points: Obviously 4 points: Strongly 5 points: Unbearable.
Claims (1)
止された肥料組成物 廃白土:植物油脂の脱色処理に使用して脱色能
が減退した活性白土を熱処理して得られる廃
白土 2 特許請求の範囲第1項記載の肥料組成物にお
いて、廃白土が、植物油脂の脱色処理に使用して
脱色能が減退した活性白土を、100〜400℃の温度
下に間接的に加熱することにより得られたもので
あることを特徴とする肥料組成物。[Scope of Claims] 1. Fertilizer composition that is prevented from caking and is made by adding the following waste white clay to the fertilizer ingredients. Waste white clay: obtained by heat treating activated white clay whose decolorizing ability has decreased after being used for decolorizing vegetable oils and fats. Waste white clay 2 In the fertilizer composition according to claim 1, the waste white clay is activated clay whose decolorizing ability has decreased after being used for the decolorization treatment of vegetable oils, and is indirectly heated at a temperature of 100 to 400°C. A fertilizer composition characterized in that it is obtained by heating.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56159715A JPS5860688A (en) | 1981-10-07 | 1981-10-07 | fertilizer composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56159715A JPS5860688A (en) | 1981-10-07 | 1981-10-07 | fertilizer composition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5860688A JPS5860688A (en) | 1983-04-11 |
| JPH021799B2 true JPH021799B2 (en) | 1990-01-12 |
Family
ID=15699697
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56159715A Granted JPS5860688A (en) | 1981-10-07 | 1981-10-07 | fertilizer composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5860688A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63260889A (en) * | 1987-04-17 | 1988-10-27 | 電気化学工業株式会社 | Solidification preventing material |
-
1981
- 1981-10-07 JP JP56159715A patent/JPS5860688A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5860688A (en) | 1983-04-11 |
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