JPS5827980B2 - Manufacturing method of granular compound fertilizer - Google Patents

Manufacturing method of granular compound fertilizer

Info

Publication number
JPS5827980B2
JPS5827980B2 JP9182079A JP9182079A JPS5827980B2 JP S5827980 B2 JPS5827980 B2 JP S5827980B2 JP 9182079 A JP9182079 A JP 9182079A JP 9182079 A JP9182079 A JP 9182079A JP S5827980 B2 JPS5827980 B2 JP S5827980B2
Authority
JP
Japan
Prior art keywords
granulation
parts
fertilizer
methionine
granular compound
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
Application number
JP9182079A
Other languages
Japanese (ja)
Other versions
JPS5615834A (en
Inventor
脩 秋月
起八郎 小玉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo Chemical Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP9182079A priority Critical patent/JPS5827980B2/en
Publication of JPS5615834A publication Critical patent/JPS5615834A/en
Publication of JPS5827980B2 publication Critical patent/JPS5827980B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は粒状複合肥料の製造方法、特に粒状複合肥料の
造粒方法の改良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a granular compound fertilizer, and particularly to an improvement in a method for granulating a granular compound fertilizer.

粒状複合肥料は一般にリン安、硫安、塩化加里、尿素等
の粉状肥料原料を各種肥料銘柄に応じて配合し、水また
は/および酸、アンモニア、ベントナイト等の造粒剤の
共存下にドラム型造粒機、皿型造粒機、パグミル等の造
粒機により製造されている。
Granular compound fertilizers are generally made by blending powdered fertilizer raw materials such as ammonium phosphorous, ammonium sulfate, potassium chloride, and urea according to various fertilizer brands, and then molding them into a drum shape in the coexistence of water and/or granulating agents such as acid, ammonia, and bentonite. It is manufactured using granulators such as granulators, dish granulators, and pug mills.

造粒品は次いで乾燥処理後篩別され、製品粒径粒子は取
出される一方篩上品は粉砕後部下品と共に循環量として
配合機又は造粒機に直接戻入されているのが普通である
The granulated product is then dried and then sieved, and the product size particles are removed, while the sieved product is usually returned directly to the blender or granulator as a circulating quantity together with the crushed lower product.

しかしながら我が国のように少量で多銘柄の肥料の製造
を行わなければならない現状においては、各銘柄毎に使
用される肥料原料の種類に応じて造粒性に難易の差が生
じるため、各銘柄ごとに造粒機内の水分、温度および肥
料原料の粒度、造粒後の戻り粉等を微妙に調整して造粒
を行なわなければならず、操作上きわめて繁雑性を有し
ていた。
However, in the current situation like Japan, where we have to manufacture many brands of fertilizer in small quantities, there are differences in the difficulty of granulation depending on the type of fertilizer raw material used for each brand. In addition, the moisture and temperature in the granulator, the particle size of the fertilizer raw material, the return powder after granulation, etc. must be delicately adjusted to perform granulation, making the operation extremely complicated.

特に、塩安、または硫安と塩化加里を原料とする窒素−
加重系肥料や溶成リン肥を主原料とする肥料を製造する
場合には、造粒が非常に困難であり、水分を与えても十
分な造粒ができないという欠点があった。
In particular, nitrogen made from ammonium chloride or ammonium sulfate and potassium chloride.
When producing fertilizers based on weighted fertilizers or dissolved phosphorus fertilizers, granulation is extremely difficult, and even when water is added, sufficient granulation cannot be achieved.

従来、このような肥料の造粒に関して、操作上の繁雑性
を解消するために種々の造粒剤が開発されているが、ま
だ十分な造粒剤は見当らない。
Conventionally, various granulating agents have been developed to solve the operational complexity of granulating such fertilizers, but a sufficient granulating agent has not yet been found.

本発明者等は、このような従来から製造されている粒状
複合肥料のもつ欠点を解消すべく種々検討した結果、以
下に述べる改良法を発明した。
The present inventors conducted various studies to solve the drawbacks of conventionally produced granular compound fertilizers, and as a result, they invented the improved method described below.

本発明方法によれば粒状複合肥料の製造において、特に
造粒困難な銘柄肥料に対しても造粒の程度を著しく向上
させ、又は/および造粒操作上の繁雑性を大幅に減少さ
せることができる。
According to the method of the present invention, in the production of granular composite fertilizer, it is possible to significantly improve the degree of granulation even for branded fertilizers that are particularly difficult to granulate, and/or significantly reduce the complexity of the granulation operation. can.

本発明方法は、各種肥料物質に対してメチオニンまたは
メチオニンの塩(たとえばカルシウム塩)を添加配合し
造粒することからなる粒状複合肥料の製造方法である。
The method of the present invention is a method for producing a granular composite fertilizer, which comprises adding and blending methionine or a methionine salt (eg, calcium salt) to various fertilizer substances and granulating the mixture.

本発明方法によって製造される粒状複合肥料としては、
原料物質の組み合わせにより、窒素−加重、窒素−リン
酸、およびリン酸−加重の2成分系、窒素−リン酸−加
重の3成分系、あるいはこれらにマグネシウム、硼素、
マンガン等植物の生育に必要な要素を含有させた粒状複
合肥料が挙げられる。
The granular compound fertilizer produced by the method of the present invention includes:
Depending on the combination of raw materials, a two-component system of nitrogen-weighted, nitrogen-phosphoric acid, and phosphoric acid-weighted, a three-component system of nitrogen-phosphoric acid-weighted, or a combination of magnesium, boron,
Examples include granular compound fertilizers containing elements necessary for plant growth, such as manganese.

本発明方法におけるメチオニンまたはその塩の添加量は
製品肥料100重量部に対して1重量部以上、好ましく
は2重量部以上使用され、製品組成、および希望する粒
径によって適宜調節される。
The amount of methionine or its salt added in the method of the present invention is 1 part by weight or more, preferably 2 parts by weight or more per 100 parts by weight of the product fertilizer, and is appropriately adjusted depending on the product composition and desired particle size.

添加量は上記量以上であれば特に制約されることは少な
いが、経済性および造粒性の面から一般に製品肥料10
0重量部あたり8重量部以上多量に用いることは好まし
いこととはいえない。
There are few restrictions on the amount added as long as it is above the above amount, but from the viewpoint of economy and granulation, generally the product fertilizer is 10
It cannot be said that it is preferable to use a large amount of 8 parts by weight or more per 0 parts by weight.

また、添加方法は特に限定されるものではなく、各種肥
料銘柄に応じて配合された粉体原料、および造粒後戻り
粉とともに造ね機に装入させることにより行なわれる。
Further, the method of addition is not particularly limited, and it is carried out by charging the powder into a granulation machine together with powder raw materials blended according to various fertilizer brands and return powder after granulation.

本発明方法の最も特徴とするところは、従来の粒状複合
肥料の造粒方法において、メチオニンまたはその塩を造
粒促進剤とするという簡単な方法により、従来より造粒
が困難とされていた、塩安または硫安と塩加を原料とす
る窒素−加重系肥料や、熔ff1Jン肥を主原料とする
粒状肥料をも容易に、しかも高収率で得ることができる
という点にある。
The most distinctive feature of the method of the present invention is that in the conventional granulation method of granular compound fertilizer, methionine or its salt is used as a granulation accelerator, which is a simple method. Nitrogen-weighted fertilizers using ammonium chloride or ammonium sulfate and salt as raw materials, and granular fertilizers using molten fertilizer as main raw materials can also be easily obtained at high yields.

このメチオニンまたはその塩の造粒促進効果についてシ
ま、メチオニンまたはその塩カ造粒時に他の粉状肥料物
質の表面に付着して粘性を与え、肥料物質間の粘着力を
増加させるために造粒促進効果を呈するものと考えられ
る。
Regarding the granulation-promoting effect of methionine or its salt, the methionine or its salt adheres to the surface of other powdered fertilizer substances during granulation to give viscosity and increase the adhesion between fertilizer substances. It is thought that it has a grain promoting effect.

また、造粒促進*剤として使用されるメチオニンまたは
その塩はそれ自身飼料として使用せられているものであ
り、農作物に対しての害はない。
In addition, methionine or its salt used as a granulation accelerator* is used as feed itself and is not harmful to agricultural crops.

以下、本発明を実施例により説明するが本発明はこれら
実施例により何ら限定されるものではない。
EXAMPLES The present invention will be explained below with reference to Examples, but the present invention is not limited to these Examples in any way.

又、実施例中に示した%は特記しない限りすべて重量%
である。
In addition, all percentages shown in the examples are by weight unless otherwise specified.
It is.

実施例 工 直径0.677+、深さ0.1.5 mの皿型造粒機を
使用して一ド記成分を有する尿素系粒状複合肥料を製造
した。
Example A urea-based granular composite fertilizer having one ingredient was produced using a dish-type granulator with a diameter of 0.677+ and a depth of 0.1.5 m.

すなわち皿型造粒機に硫安(N:21%)389部、塩
化加重(K2O:61%)290部、ウラホルム(N:
40%)100部、オリビンサンド60部に、造粒促進
剤としてメチオニン33部を供給混合し、この固体混合
物を加熱して70℃まで上昇させた後。
That is, 389 parts of ammonium sulfate (N: 21%), 290 parts of chloride weighted (K2O: 61%), and Uraform (N:
40%) and 60 parts of olivine sand were mixed with 33 parts of methionine as a granulation accelerator, and the solid mixture was heated to 70°C.

98%硫酸93部、水65部をスプレー添加しながらア
ンモニアガス32部を供給して回転数24rpm、造粒
時間5分間の条件下で造粒した。
While spraying 93 parts of 98% sulfuric acid and 65 parts of water, 32 parts of ammonia gas was supplied, and granulation was carried out at a rotation speed of 24 rpm and a granulation time of 5 minutes.

※比較のため、メチオ
ニンを添加しない場合と、造粒促進剤としてベントナイ
ト33部を添加した場合について同様の方法で造粒した
*For comparison, granulation was carried out in the same manner in the case where methionine was not added and in the case where 33 parts of bentonite was added as a granulation accelerator.

これら本発明による方法および比較例の方法による造粒
品の粒度および硬度は第1表の如くであり、本発明の方
法によれば比較例の方法よりも硬度を低下させることな
く造粒性を格段に向上できることが認められた。
The particle size and hardness of the granulated products obtained by the method of the present invention and the method of the comparative example are as shown in Table 1. It was recognized that significant improvements could be made.

実施例 2 実施例1に記載した方法と同様の方法で下記成分を有す
る尿素系粒状複合肥料を製造した。
Example 2 A urea-based granular composite fertilizer having the following components was produced in the same manner as described in Example 1.

N N P2O5 K20 (%)2010 12 12 皿型造粒機に硫安(N:21%)218部、塩化加重(
K2O:61%)208部、尿素(uN:46%)21
7部、オリビンサンド21部に、造粒促進剤としてメチ
オニン33部を供給混合し、この固体混合物を加熱して
70’Cまで上昇させた後、別途、湿式リン酸(P2O
5:38%、H25O41%)332部にアンモニアガ
ス46部を供給して得た燐安スラリを上記固体混合物に
添加混合し、98%硫酸45部をスプレー添加しながら
アンモニアガス30部を供給して回転数24rpm、造
粒時間5分間の条件下で造粒した。
N N P2O5 K20 (%) 2010 12 12 218 parts of ammonium sulfate (N: 21%), chloride weight (
K2O: 61%) 208 parts, urea (uN: 46%) 21
7 parts and 21 parts of olivine sand are mixed with 33 parts of methionine as a granulation accelerator, and after heating this solid mixture to 70'C, wet phosphoric acid (P2O
Phosphoric ammonium slurry obtained by supplying 46 parts of ammonia gas to 332 parts of 5:38% H25O41%) was added and mixed to the above solid mixture, and 30 parts of ammonia gas was supplied while spraying 45 parts of 98% sulfuric acid. The pellets were granulated at a rotation speed of 24 rpm and a granulation time of 5 minutes.

比較のため、メチオニンを添加しない場合と造粒促進剤
としてベントナイト33部を添加した場合について同様
の方法で造粒した。
For comparison, granulation was carried out in the same manner in the case where methionine was not added and in the case where 33 parts of bentonite was added as a granulation accelerator.

結束を第2表に示す。The binding is shown in Table 2.

Claims (1)

【特許請求の範囲】[Claims] 1 各種肥料物質に対し造粒促進剤としてメチオニンま
たはメチオニンの塩を添加し、造粒することを特徴とす
る粒状複合肥料の製造方法。
1. A method for producing a granular compound fertilizer, which comprises adding methionine or methionine salt as a granulation accelerator to various fertilizer substances and granulating the mixture.
JP9182079A 1979-07-18 1979-07-18 Manufacturing method of granular compound fertilizer Expired JPS5827980B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9182079A JPS5827980B2 (en) 1979-07-18 1979-07-18 Manufacturing method of granular compound fertilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9182079A JPS5827980B2 (en) 1979-07-18 1979-07-18 Manufacturing method of granular compound fertilizer

Publications (2)

Publication Number Publication Date
JPS5615834A JPS5615834A (en) 1981-02-16
JPS5827980B2 true JPS5827980B2 (en) 1983-06-13

Family

ID=14037254

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9182079A Expired JPS5827980B2 (en) 1979-07-18 1979-07-18 Manufacturing method of granular compound fertilizer

Country Status (1)

Country Link
JP (1) JPS5827980B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19707380A1 (en) 1997-02-25 1998-08-27 Degussa Process for producing a free-flowing animal feed supplement based on methionine salt and the granules obtainable in this way
EP3461803A1 (en) * 2017-10-02 2019-04-03 Evonik Degussa GmbH Method for the production of granules containing dipeptide

Also Published As

Publication number Publication date
JPS5615834A (en) 1981-02-16

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