JP2001031488A - Production of fertilizer and solid fertilizer - Google Patents
Production of fertilizer and solid fertilizerInfo
- Publication number
- JP2001031488A JP2001031488A JP2000021269A JP2000021269A JP2001031488A JP 2001031488 A JP2001031488 A JP 2001031488A JP 2000021269 A JP2000021269 A JP 2000021269A JP 2000021269 A JP2000021269 A JP 2000021269A JP 2001031488 A JP2001031488 A JP 2001031488A
- Authority
- JP
- Japan
- Prior art keywords
- fertilizer
- urea
- solid
- potassium
- weight
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G1/00—Mixtures of fertilisers belonging individually to different subclasses of C05
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05C—NITROGENOUS FERTILISERS
- C05C9/00—Fertilisers containing urea or urea compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Pest Control & Pesticides (AREA)
- Fertilizers (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、肥料の製造方法お
よび固体肥料に存する。詳しくは、肥料の主成分である
窒素、リン酸及びカリウム成分の合計量が多い肥料の製
造方法とその固体肥料に存する。The present invention relates to a method for producing a fertilizer and a solid fertilizer. Specifically, the present invention relates to a method for producing a fertilizer having a large total amount of nitrogen, phosphoric acid and potassium components, which are main components of the fertilizer, and a solid fertilizer thereof.
【0002】[0002]
【従来の技術】近年、農業人口は減少傾向にあり、加え
て就業人口の平均年齢の老齢化の進行により作業の省力
化が求められており、特に施肥労力の軽減が求められて
いる。肥料における成分の中でも、とりわけ窒素成分は
例えば水稲等の農作物の生育にとって重要な肥料成分で
あり、その施肥は農作物の生育期間全般を通じて必要と
されるので、効率の良い省力的な施肥に適した肥料が求
められてきた。2. Description of the Related Art In recent years, the agricultural population has been declining, and in addition, the average age of the working population has been aging, so that labor has been required to be reduced, and in particular, the fertilization labor has been required to be reduced. Among the components in the fertilizer, the nitrogen component is an important fertilizer component for growing crops such as paddy rice, and the fertilization is required throughout the growing season of the crop, so it is suitable for efficient and labor-saving fertilization. Fertilizer has been sought.
【0003】従来よりこの様な問題を解決すべく、施肥
回数を軽減するために、肥料の単位重量当たり窒素、リ
ン酸及びカリウム成分(以下、「NPK成分」と言うこ
とがある。)の含有量を多くした、いわゆる高度化成肥
料の開発がなされてきた。従来、このようなものは液体
であることが多かったが、さらにはこれを固体化するこ
とで、液体肥料(液肥)に比べて軽量化された肥料の開
発もなされてきた。Conventionally, in order to solve such a problem, in order to reduce the number of times of fertilization, nitrogen, phosphoric acid and potassium components (hereinafter may be referred to as "NPK components") per unit weight of fertilizer are contained. So-called advanced chemical fertilizers have been developed in large amounts. In the past, such materials were often liquids, but furthermore, solidification of such materials has led to the development of fertilizers that are lighter than liquid fertilizers (liquid fertilizers).
【0004】高度化成肥料の製造には、尿素、硫安、硝
安などの窒素質肥料と、過燐酸石灰などの燐酸質肥料、
塩化カリウム等のカリウム質肥料を、反応又は混合する
ことにより製造する方法がある。この製造においては、
その反応条件や各成分の混合比率を変えることにより、
NPK成分における成分比率(NPK成分比)を変える
ことが出来る。この例として、特開昭50−99816
号公報、同51−118000号公報等にNPK成分が
60%以上という高度化成肥料の製造方法の記載があ
る。また高度化成肥料は、肥料成分の比率が高い(副成
分の比率が低い)ので、例えば硫酸塩等の副成分による
土壌への悪影響、土壌の酸性化などが起こりにくい傾向
を有する。In the production of advanced chemical fertilizers, nitrogenous fertilizers such as urea, ammonium sulfate and ammonium nitrate, and phosphate fertilizers such as lime superphosphate,
There is a method of producing a potassium fertilizer such as potassium chloride by reacting or mixing. In this production,
By changing the reaction conditions and the mixing ratio of each component,
The component ratio (NPK component ratio) in the NPK component can be changed. An example of this is disclosed in Japanese Patent Laid-Open No. 50-99816.
No. 5,111,8000, etc., there is a description of a method for producing an advanced chemical fertilizer having an NPK component of 60% or more. In addition, advanced chemical fertilizers have a high ratio of fertilizer components (a low ratio of subcomponents), and thus have a tendency that adverse effects on soil, acidification of soil, and the like due to subcomponents such as sulfates are unlikely to occur.
【0005】[0005]
【発明が解決しようとする課題】しかし従来の高度化成
肥料の製造方法の多くでは、原料に含まれる硫酸根、塩
酸根等の副成分が製品に混入してしまうので、NPK成
分の含有量は50%に満たないものであった。例えば特
公昭59−19909号公報等には窒素成分の含有量を
増加させる方法の記載があるが、窒素成分を上げること
でリン酸及びカリウム成分の含有率が下がり、結果とし
てNPK成分が50%に満たないものとなってしまって
いる。且つ、この様な副成分の存在によって、施肥した
土壌の酸性化を促進してしまう恐れがあった。また先述
の特開昭50−99816号公報や同51−11800
0号公報等に記載の製造方法では、いずれも製造条件が
150℃〜800℃という高温であるため製造コストが
高くなり、最終製品の肥料が非常に高価なものになって
しまうという欠点があった。また特開昭50−9981
6号公報等にも肥料の製造方法に関する記載があるが、
製造原料に高価なメタリン酸カリを使用しており、これ
もまた、最終製品の肥料が非常に高価なものになってし
まうという欠点があった。However, in many of the conventional methods for producing advanced chemical fertilizers, secondary components such as sulfates and hydrochlorides contained in the raw materials are mixed into the product, so that the content of the NPK component is reduced. It was less than 50%. For example, Japanese Patent Publication No. 59-19909 discloses a method of increasing the content of a nitrogen component. The content of a phosphoric acid and a potassium component is decreased by increasing the nitrogen component. As a result, the NPK component is reduced to 50%. It has become less than. In addition, there is a possibility that the acidification of the fertilized soil may be promoted by the presence of such subcomponents. Also, the aforementioned Japanese Patent Application Laid-Open Nos. 50-99816 and 51-11800.
In the production methods described in Japanese Patent Application Publication No. 0-203, etc., the production conditions are all high, such as 150 ° C. to 800 ° C., so that the production cost is high, and the fertilizer of the final product is extremely expensive. Was. Japanese Patent Laid-Open No. 50-9981
No. 6 also discloses a method for producing fertilizer,
Since expensive potassium metaphosphate is used as a raw material for production, there is also a disadvantage that the fertilizer of the final product becomes very expensive.
【0006】加えて、先述の通り窒素成分は農作物の生
育に重要であるので、従来の高度化成肥料においても、
肥料全体における窒素成分含有率のさらなる向上が要求
されていた。しかし窒素成分の含有量を上げる為の検討
として、その多くは安価で且つ窒素成分の高い尿素を用
いる方法が検討されてきたので、尿素の持つ強い吸湿性
により、安定な、吸湿性の低い固体肥料の製造は困難で
あった。更に、例えば特公昭61−5679号公報や特
公昭51−40877号公報には、鉄及び/又はアルミ
ニウムを含む肥料の製造方法が記載されているが、これ
らの方法では鉄及び/又はアルミニウムを含む塩類等を
肥料の製造工程において単純混合するのみなので、製品
中の品質ムラが問題となっていた。[0006] In addition, as described above, the nitrogen component is important for the growth of agricultural crops.
Further improvement in the nitrogen content of the entire fertilizer was required. However, in order to increase the content of the nitrogen component, many of the methods using inexpensive and high-nitrogen components urea have been studied. Manufacture of fertilizer was difficult. Furthermore, for example, Japanese Patent Publication Nos. 61-5679 and 51-40877 describe methods for producing fertilizers containing iron and / or aluminum. Since salts and the like are simply mixed in the fertilizer production process, quality unevenness in the product has been a problem.
【0007】[0007]
【課題を解決するための手段】上述してきた実状に鑑み
本発明者は鋭意検討した結果、安価なウレアホスフェイ
トとカリウム化合物を水の存在下で反応させることによ
って、緩やかな反応条件下において、硫酸根等の土壌に
悪影響を及ぼす副成分の含有量を低く抑え、かつ吸湿性
の改善された高度化成肥料を安価に製造することを見い
出し、本発明を完成させた。また、好ましくは鉄及び/
又はアルミニウムを含有するウレアホスフェイトとカリ
ウム化合物を反応させることで、鉄及び/又はアルミニ
ウムのリン酸塩を非晶質固体として反応系全体に均一に
分散させることが出来、前述の諸効果をより高めること
が可能となった。さらに本発明の固体肥料は、特定元素
を含有させることによって、窒素成分の含有量が20%
以上の高度化成肥料で且つ吸湿性の抑制された固体肥料
を提供するものであり、液肥に対して軽量化され、施肥
作業の省力化に貢献するものである。Means for Solving the Problems In view of the above-mentioned situation, the present inventors have conducted intensive studies and have found that by reacting inexpensive urea phosphate with a potassium compound in the presence of water, under mild reaction conditions, The present inventors have found that the content of secondary components that adversely affect the soil such as sulfate groups is kept low and that an advanced chemical fertilizer with improved hygroscopicity is produced at low cost, and the present invention has been completed. Preferably, iron and / or
Alternatively, by reacting a potassium compound with a urea phosphate containing aluminum, the phosphate of iron and / or aluminum can be uniformly dispersed as an amorphous solid throughout the reaction system, and the above-described effects can be improved. It became possible to increase. Furthermore, the solid fertilizer of the present invention has a nitrogen content of 20% by containing a specific element.
The present invention provides a solid fertilizer which is the above-mentioned advanced chemical fertilizer and whose hygroscopicity is suppressed, which is lighter than liquid fertilizer and contributes to labor saving in fertilization work.
【0008】本発明の要旨は、ウレアホスフェイト(以
下、UPと略記することがある)とカリウム化合物とを
水の存在下で反応させることを特徴とする肥料の製造方
法に存する。又、本発明の今一つの要旨は、窒素成分、
リン酸成分およびカリウム成分の合計が50重量%以上
であり、鉄及び/又はアルミニウムの含有量が0.01
〜10重量%である固体肥料、特に窒素成分が20重量
%以上であることを特徴とする固体肥料に存する。尚、
本発明に於いては、肥料のNPK成分比(窒素、リン
酸、カリウム成分の比)について、肥料中における各要
素をN、P2 O5 及びK2 Oに換算して、肥料重量に対
する重量%として表記する。例えば、NPK成分におい
て各々の重量%が10重量%の際は、10−10−10
と記す。The gist of the present invention resides in a method for producing a fertilizer, comprising reacting a urea phosphate (hereinafter sometimes abbreviated as UP) with a potassium compound in the presence of water. Further, another gist of the present invention is a nitrogen component,
The total of the phosphoric acid component and the potassium component is 50% by weight or more, and the content of iron and / or aluminum is 0.01%.
-10% by weight of a solid fertilizer, particularly a solid fertilizer characterized in that a nitrogen component is 20% by weight or more. still,
In the present invention, regarding the NPK component ratio (ratio of nitrogen, phosphoric acid, and potassium components) of the fertilizer, each element in the fertilizer is converted into N, P2O5, and K2O, and is expressed as% by weight based on the weight of the fertilizer. I do. For example, when each weight% of the NPK component is 10 weight%, 10-10-10
It is written.
【0009】[0009]
【発明の実施の形態】以下、本発明を詳細に説明する。 I:肥料の製造方法 本発明においては、ウレアホスフェイト(UP)とカリ
ウム化合物とを水の存在下で反応させることで、NPK
成分の高い肥料を製造できる。本発明に用いるUPは乾
式燐酸と尿素とを反応させる方法や、湿式燐酸と尿素と
反応させる方法等、任意の製造方法で得られたものを使
用できる。中でも湿式燐酸と尿素とを反応させて得られ
たUPを用いることによって、得られる肥料が、NPK
成分が高く吸湿性の低い固体肥料となり、例えばNPK
成分が13−35−25の様な固体の高度化成肥料を製
造する上で好ましい。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail. I: Production Method of Fertilizer In the present invention, NPK is produced by reacting urea phosphate (UP) with a potassium compound in the presence of water.
Manufacture of fertilizer with high components. As the UP used in the present invention, those obtained by any production method such as a method of reacting dry phosphoric acid with urea and a method of reacting wet phosphoric acid with urea can be used. Above all, by using UP obtained by reacting wet phosphoric acid and urea, the fertilizer obtained can be NPK
It becomes a solid fertilizer with high components and low hygroscopicity, such as NPK
The component is preferable in producing a solid advanced chemical fertilizer such as 13-35-25.
【0010】本発明におけるUPとカリウム化合物との
反応条件は適宜設定すれば良いが、本発明においては反
応自体が発熱反応のため、特に高温、高圧下の様な厳し
い条件とせずとも水を存在させることによって反応が進
行するので、工業上有利である。反応条件としては通
常、10〜120℃、中でも40〜100℃とするのが
好ましく、反応時間は2〜20分、好ましくは5〜10
分である。反応系内の水分量は、用いるUPやカリウム
化合物の量などによって適宜選択すればよいが、通常は
0.1〜80重量%、中でも1〜60重量%、特に2〜
20重量%の範囲とするのが好ましい。水分量が1重量
%に満たない場合には、乾燥状態の固体UPと固体カリ
ウム化合物が激しく反応し、その発熱反応によりアンモ
ニアを発生しながらUPが分解してしまうことがある。
反応系への水の添加は、各原料と水を別々に添加して
も、各原料を水溶液又は水性スラリーの形態で添加する
ことにより行なってもよい。用いるウレアホスフェイト
としては、鉄及び/又はアルミニウムを0.01〜20
重量%含むことが好ましい。例えば正リン酸と尿素を反
応させて得られたウレアホスフェイトに鉄及び/又はア
ルミニウムを塩や錯体等の形で添加してもよいし、また
その反応原料中に所望量を添加して用いてもよい。中で
も以下に述べるような湿式燐酸と尿素との反応によって
得る方法は湿式燐酸中の鉄及び/又はアルミニウムを利
用でき、添加等の工程が省略できるので特に好ましい。In the present invention, the conditions for the reaction between the UP and the potassium compound may be appropriately set. However, in the present invention, since the reaction itself is an exothermic reaction, water is present even without severe conditions such as high temperature and high pressure. The reaction proceeds by causing the reaction, which is industrially advantageous. The reaction conditions are usually 10 to 120 ° C., preferably 40 to 100 ° C., and the reaction time is 2 to 20 minutes, preferably 5 to 10 minutes.
Minutes. The amount of water in the reaction system may be appropriately selected depending on the amount of the UP or potassium compound used, but is usually 0.1 to 80% by weight, preferably 1 to 60% by weight, particularly 2 to 2% by weight.
Preferably, it is in the range of 20% by weight. If the water content is less than 1% by weight, the dry solid UP and the solid potassium compound react violently, and the exothermic reaction may generate ammonia to decompose the UP.
Water may be added to the reaction system by adding each raw material and water separately or by adding each raw material in the form of an aqueous solution or an aqueous slurry. As the urea phosphate to be used, iron and / or aluminum is used in an amount of 0.01 to 20.
It is preferred that the content be contained by weight. For example, iron and / or aluminum may be added in the form of a salt or complex to urea phosphate obtained by reacting orthophosphoric acid and urea, or a desired amount may be added to the reaction raw material. You may. Above all, a method obtained by a reaction between wet phosphoric acid and urea as described below is particularly preferable because iron and / or aluminum in wet phosphoric acid can be used and steps such as addition can be omitted.
【0011】UPとカリウム化合物との反応において、
各々反応物に用いる原料の形態は固体や溶液等、適宜選
択すればよい。なお本発明における溶液とは、溶質が完
全溶解した、いわゆる水溶液等の溶液のみならず、一部
未溶解の溶質を含む、分散液やスラリー状流動体をも含
むものである。UPとカリウム化合物との反応に於いて
は、通常、水性媒体中で行なわれるが、このうち以下に
示す(1)〜(3)の方法が好ましい。 (1)湿式燐酸と尿素との反応混合物から濾別した固形
物の溶液と、固体カリウム化合物又はその溶液とを反応
させる。 (2)湿式燐酸と尿素との反応混合物から濾別した固形
物に、カリウム化合物溶液を添加し反応させる。 (3)湿式燐酸と尿素との反応混合物から濾別した固形
物を、カリウム化合物溶液を添加し反応させる。In the reaction between UP and a potassium compound,
The form of the raw material used for each reactant may be appropriately selected, such as a solid or a solution. The solution in the present invention includes not only a solution such as a so-called aqueous solution in which a solute is completely dissolved, but also a dispersion or a slurry-like fluid containing a partially undissolved solute. The reaction between the UP and the potassium compound is usually carried out in an aqueous medium, but the following methods (1) to (3) are preferred. (1) A solution of a solid substance filtered from a reaction mixture of wet phosphoric acid and urea is reacted with a solid potassium compound or a solution thereof. (2) A potassium compound solution is added to and reacted with a solid that has been filtered from the reaction mixture of wet phosphoric acid and urea. (3) The solid substance filtered off from the reaction mixture of wet phosphoric acid and urea is reacted by adding a potassium compound solution.
【0012】例えば(1)の方法の1つとして、主にU
Pである、湿式燐酸と尿素との反応混合物から濾別した
固形物(以下、単に固形物と言うことがある。)を溶媒
に水やアルコールを用いて溶液とし、これとカリウム化
合物溶液と反応させる方法がある。この方法では通常、
固形物を水溶液又水性スラリーとして用い、カリウム化
合物は水溶液として用いるのが好ましい。特に固形物は
水性スラリーとすることで反応が速やかに進むので好ま
しい。この方法だと反応系に溶媒、好ましくは水が多く
存在するので、反応生成物を直接、噴霧乾燥を行うこと
で固体肥料を容易に製造することが出来る。尚、この
時、カリウム化合物溶液は滴下等ゆっくり添加すること
が好ましい。For example, as one of the methods (1), mainly U
A solid substance (hereinafter, may be simply referred to as a solid substance) filtered from a reaction mixture of wet phosphoric acid and urea, which is P, is converted into a solution using water or an alcohol as a solvent, and is reacted with a potassium compound solution. There is a way to make it happen. This method usually uses
The solid is preferably used as an aqueous solution or an aqueous slurry, and the potassium compound is preferably used as an aqueous solution. Particularly, a solid material is preferable because the reaction proceeds promptly by using an aqueous slurry. According to this method, a large amount of a solvent, preferably water, is present in the reaction system. Therefore, a solid fertilizer can be easily produced by directly spray-drying the reaction product. At this time, it is preferable that the potassium compound solution is slowly added by dropping or the like.
【0013】また(1)の別の方法としては、固形物の
溶液と、固体のカリウム化合物とを反応させる方法があ
る。この方法では、反応系に存在する溶媒、好ましくは
水が先述の方法より少なく、生成物における肥料の濃度
が高く、例えば粘性を有するゲル状物として得られる。
よって、これを乾燥して固体肥料を得る場合には薄膜状
にして乾燥するなどの手段により容易に固体肥料を得る
ことが出来る。更に別の方法として(2)や(3)の様
に、固形物をそのまま、カリウム化合物溶液と反応させ
る方法がある。この方法では通常、カリウム化合物は水
溶液として用いるのが好ましい。この方法では、反応系
に溶媒、好ましくは水が従前の反応方法と同様に少な
く、生成物における肥料成分の濃度が高く、例えば粘性
を有するゲル状物または水分が更に少ないと塊状物とし
て得られる。よって、この方法に於いては乾燥が不要と
なる場合があるが、乾燥して固体肥料を得る場合には、
先述と同様の方法によればよい。As another method (1), there is a method of reacting a solid solution with a solid potassium compound. In this method, the amount of the solvent, preferably water, present in the reaction system is smaller than that of the above-mentioned method, and the concentration of the fertilizer in the product is high, for example, a viscous gel is obtained.
Therefore, when the solid fertilizer is obtained by drying the solid fertilizer, the solid fertilizer can be easily obtained by means such as a thin film and drying. As still another method, there is a method in which a solid is reacted with a potassium compound solution as it is, as in (2) and (3). In this method, the potassium compound is usually preferably used as an aqueous solution. In this method, the solvent in the reaction system, preferably water, is low as in the previous reaction method, and the concentration of the fertilizer component in the product is high. For example, a viscous gel or a mass with less water is obtained as a mass. . Therefore, drying may not be necessary in this method, but when drying to obtain solid fertilizer,
The same method as described above may be used.
【0014】尚、これらの方法では、(2)固形物にカ
リウム化合物溶液を滴下等によって反応させる方法と、
(3)カリウム化合物溶液に固形物を添加して反応させ
る方法とがあるが、反応熱によりUPの分解が生じ難
い、(2)の方法の方がより好ましく、また固形物にカ
リウム化合物を溶液を少しずつ添加することが好まし
い。本発明においては、湿式燐酸は燐鉱石を硫酸または
硫燐酸の混酸で分解して得るような一般的方法により得
られたものを使用でき、尿素も又同様にその製造方法は
任意である。湿式燐酸と尿素を反応させる際の量比は通
常、湿式燐酸1モルに対し、尿素が0.1〜2モル、中
でも0.5〜1.5モル、特に0.8〜1.5モルが好
ましい。反応時間は通常1〜30分であり、反応温度を
尿素の分解温度以下に調整しつつ行うことが好ましい。
尿素が0.1モル以下だと反応速度が遅くなることがあ
り、又1.5モル以上ではリン酸と未反応の尿素が後述
するように生成したUPを濾別する際の母液に移行し、
歩留まりが悪化することがある。反応に用いる尿素の形
態は固体、又は水溶液やスラリー等、任意であるが、反
応時間を短縮するためにスラリー又は固体尿素を直接湿
式燐酸と反応させることが好ましい。尿素を液体で用い
る場合、反応時間は10分以上かかる場合があるが、ス
ラリーを用いると反応時間が1〜5分に、又固体尿素を
直接湿式燐酸と反応させると、場合により反応時間が1
分以下となるので好ましい。尚、後述するように生成し
たUPを濾別する際の母液を少なくする意味でも、固体
尿素を用いるのが好ましい。In these methods, (2) a method in which a potassium compound solution is reacted with a solid substance by dropping or the like;
(3) There is a method in which a solid is added to the potassium compound solution to cause a reaction, but UP is less likely to be decomposed due to reaction heat, and the method in (2) is more preferable. Is preferably added little by little. In the present invention, as the wet phosphoric acid, those obtained by a general method such as that obtained by decomposing phosphate rock with sulfuric acid or a mixed acid of sulfuric phosphoric acid can be used, and the production method of urea is also arbitrary. The amount ratio of the wet phosphoric acid to urea is usually 0.1 to 2 mol, preferably 0.5 to 1.5 mol, particularly 0.8 to 1.5 mol per 1 mol of wet phosphoric acid. preferable. The reaction time is usually from 1 to 30 minutes, and it is preferable to carry out the reaction while adjusting the reaction temperature to the urea decomposition temperature or lower.
If the amount of urea is 0.1 mol or less, the reaction rate may be reduced. If the amount of urea is 1.5 mol or more, urea unreacted with phosphoric acid migrates to the mother liquor when the generated UP is filtered out as described later. ,
Yield may deteriorate. The form of urea used for the reaction is arbitrary such as solid, aqueous solution or slurry, but it is preferable to directly react the slurry or solid urea with wet phosphoric acid to shorten the reaction time. When urea is used as a liquid, the reaction time may take 10 minutes or more. When a slurry is used, the reaction time may be 1 to 5 minutes. When solid urea is directly reacted with wet phosphoric acid, the reaction time may be 1 minute.
Minutes or less. In addition, it is preferable to use solid urea from the viewpoint of reducing the amount of mother liquor when filtering generated UP as described later.
【0015】得られたUPは、母液を濾過することで得
られる。この濾過の際に硫酸根等の肥料の副成分が、母
液とともに分離できる。本発明では次いで、上述のよう
な方法で得られたUPを水の存在下でカリウム化合物と
反応させ、肥料を製造する。本発明に用いるカリウム化
合物としては任意のカリウム化合物を用いることが出
来、例えば水酸化カリウム、カリウムメトキシド、カリ
ウムエトキシド等のカリウムアルコキシド、炭酸カリウ
ム、炭酸水素カリウム、塩化カリウム、硫酸カリウム等
のカリウム塩等が挙げられる。中でも炭酸カリウム、炭
酸水素カリウム、水酸化カリウムが好ましく、特に水酸
化カリウムが反応速度が早くかつ少ない使用量で反応が
進み、得られる肥料についても植物には有効で土壌への
悪影響が少ないという観点から好ましい。[0015] The obtained UP is obtained by filtering the mother liquor. At the time of this filtration, secondary components of fertilizer such as sulfate groups can be separated together with the mother liquor. Next, in the present invention, the UP obtained by the above method is reacted with a potassium compound in the presence of water to produce a fertilizer. As the potassium compound used in the present invention, any potassium compound can be used, for example, potassium alkoxides such as potassium hydroxide, potassium methoxide and potassium ethoxide, potassium carbonate such as potassium carbonate, potassium hydrogen carbonate, potassium chloride and potassium sulfate. And the like. Among them, potassium carbonate, potassium bicarbonate, and potassium hydroxide are preferable. Particularly, potassium hydroxide has a high reaction rate and the reaction proceeds with a small amount of use, and the resulting fertilizer is effective for plants and has little adverse effect on soil. Is preferred.
【0016】用いるカリウム化合物の量は通常、UP
1.0モルに対し、カリウム化合物中のカリウムのモル
比換算で、0.1〜2.0モル、中でも0.5〜1.5
モル、特に0.8〜1.2モルとすることが好ましい。
0.1モル未満では、得られる生成物は固体(若しくは
ゲル状)とならないことがあり、固体肥料の製造に適さ
ない場合がある。また2.0モルを超えると、同様に生
成物が固体(若しくはゲル状)とならずに、褐色の液体
になることがある。尚、これらの液体生成物は、液体肥
料(液肥)の原料として使用可能であるThe amount of the potassium compound used is usually UP
0.1 to 2.0 mol, especially 0.5 to 1.5 mol, in terms of the molar ratio of potassium in the potassium compound to 1.0 mol.
Mol, particularly preferably 0.8 to 1.2 mol.
If it is less than 0.1 mol, the resulting product may not be solid (or gel-like) and may not be suitable for producing solid fertilizer. If the amount exceeds 2.0 mol, the product may not be solid (or gel-like) but may be a brown liquid. In addition, these liquid products can be used as a raw material of liquid fertilizer (liquid fertilizer).
【0017】本発明に於いては、今まで述べてきた方法
により得られた肥料に、更に窒素成分を添加して、より
NPK成分の高い、高度化成肥料を製造することが出来
る。例えば、上述したUPとカリウム化合物との反応に
よって得られた生成物、好ましくは粘性を有するゲル状
又は塊状の生成物に、窒素成分を添加し乾燥すること
で、よりNPK成分が高く、且つ所望の窒素成分割合の
固体肥料を製造することが出来る。添加する窒素成分は
従来公知のものから適宜選択すればよいが、例えば尿
素、ジシアンジアミド、ウレアホルム、オキサミド、I
BDU(登録商標)、クロトミリデンウレア(2−オキ
ソ−4−メチル−6−ウレイドヘキサヒドロピリミジ
ン)、グアニルウレア、グアニジン、ウレア−Z、グリ
コールウリル、フルフラール尿素化合物類、シアヌル
酸、アンメリド、アンメリン、メラミン化合物類、トリ
アゾン化合物類等が挙げられる。中でも、最終的に得ら
れる高度化成固体肥料において窒素成分が20%以上の
高成分の固体肥料とするために、尿素、ジシアンジアミ
ド、グアニジン、アンメリド、メラミン化合物類、トリ
アゾン化合物類が好ましい。さらに、固体肥料の肥効面
を考慮すれば、尿素、ジシアンジアミド、グアニジンが
好ましい。In the present invention, an advanced chemical fertilizer having a higher NPK component can be produced by further adding a nitrogen component to the fertilizer obtained by the above-described method. For example, by adding a nitrogen component to a product obtained by the above-described reaction of the UP with the potassium compound, preferably a viscous gel or lump product and drying the product, the NPK component is higher and the desired The solid fertilizer having a nitrogen component ratio can be produced. The nitrogen component to be added may be appropriately selected from conventionally known ones. For example, urea, dicyandiamide, ureaform, oxamide, I
BDU (registered trademark), clotomilidene urea (2-oxo-4-methyl-6-ureidohexahydropyrimidine), guanylurea, guanidine, urea-Z, glycoluril, furfural urea compounds, cyanuric acid, ammelide, ammeline , Melamine compounds, triazone compounds and the like. Among them, urea, dicyandiamide, guanidine, ammelide, melamine compounds, and triazone compounds are preferable in order to obtain a solid fertilizer having a nitrogen component of 20% or more in the finally obtained advanced chemical solid fertilizer. Furthermore, urea, dicyandiamide, and guanidine are preferable in view of the fertilizer surface of the solid fertilizer.
【0018】添加する窒素成分の状態は適宜選択すれば
よいが、窒素成分を粒状、押し出し成形による打錠型タ
ブレット、粉末状等の固体核材として用い、UPとカリ
ウム化合物との反応によって得られた固形物、好ましく
は粘性を有するゲル状又は塊状の固形物で被覆すること
が好ましい。この様にして得られた肥料は、例えば添加
する窒素成分が尿素等の即効性の窒素成分の場合には、
その肥効をコントロールし、高度化成固体肥料を緩効化
出来るので好ましい。被覆する際の被膜の量や膜厚等
は、所望する肥料の性能に合わせて、適宜公知の方法に
より調整すればよい。また、窒素成分以外にリン成分と
してポリリン安、リン一安、リン二安等を添加しても良
い。The state of the nitrogen component to be added may be appropriately selected. The nitrogen component is used as a solid core material such as a granular tablet, a tableting tablet by extrusion, or a powder, and is obtained by a reaction between UP and a potassium compound. It is preferable to coat with a solid material, preferably a viscous gel or lump solid material. The fertilizer thus obtained is, for example, when the nitrogen component to be added is a quick-acting nitrogen component such as urea,
It is preferable because the fertilizing effect can be controlled and the advanced chemical solid fertilizer can be slowed down. The amount and film thickness of the coating at the time of coating may be appropriately adjusted by a known method according to the desired performance of the fertilizer. Further, in addition to the nitrogen component, polyphosphorus, polyanthracene, dianthine, etc. may be added as a phosphorus component.
【0019】II:固体肥料 本発明の固体肥料は、NPK成分が50重量%以上であ
り、鉄及び/又はアルミニウムが0.01〜10重量%
である固体肥料、特に窒素成分が20重量%以上である
ことを特徴とする固体肥料である。本発明の固体肥料
は、固体肥料中に鉄及び/又はアルミニウムを0.01
〜10重量%含有させることによって、高度化成肥料で
ありながら固形化することが出来、そして従来の高度化
成肥料の問題であった吸湿性の問題を解決し、水中崩壊
性に優れ、さらにはNPK成分における窒素成分を20
重量%以上と向上させることができた、優れた固体肥料
である。固体肥料中の鉄及び/又はアルミニウム含有量
は0.01〜10重量%であるが、中でも0.01〜
3.0重量%、更には0.01〜2.5重量%、特に
0.02〜1.5重量%含有させることが好ましい。
0.01重量%未満では、固体肥料の吸湿性が高くなっ
てしまい、また10重量%を越えると、固体肥料の粉化
の原因となり、また経済的ではない。本発明において
は、鉄またはアルミニウムのいずれかが0.01〜10
重量%含有されていればよいが、好ましくは、鉄および
アルミニウムを含み、その重量比は、1:9から9:
1、更に好ましくは4:6から6:4である。本発明の
固体肥料の製造方法は任意であり、従来公知の方法を用
いればよく、例えば鉄及び/又はアルミニウムを塩や錯
体等の化合物として原料に添加して製造してもよい
が、、従前の(I)にて述べた方法によって製造される
ことが好ましい。これは原料を化学反応させることによ
り肥料を製造することで肥料中にて鉄及び/又はアルミ
ニウムが非晶質固体である燐酸塩等の塩の形態をとり、
固体肥料の固形化、吸湿性の低減、水中崩壊性に優れた
効果を奏するためである。II: Solid Fertilizer The solid fertilizer of the present invention contains 50% by weight or more of NPK component and 0.01 to 10% by weight of iron and / or aluminum.
, Especially a solid fertilizer characterized in that the nitrogen component is 20% by weight or more. The solid fertilizer of the present invention contains iron and / or aluminum in the solid fertilizer in an amount of 0.01%.
By adding up to 10% by weight, it is possible to solidify the fertilizer while it is an advanced chemical fertilizer, and to solve the problem of hygroscopicity which was a problem of the conventional advanced chemical fertilizer, to have excellent disintegration in water, and to further improve NPK. 20 nitrogen components
It is an excellent solid fertilizer that could be improved to more than weight%. The iron and / or aluminum content in the solid fertilizer is 0.01 to 10% by weight, and especially 0.01 to 10% by weight.
It is preferably contained in an amount of 3.0% by weight, more preferably 0.01 to 2.5% by weight, particularly preferably 0.02 to 1.5% by weight.
If it is less than 0.01% by weight, the hygroscopicity of the solid fertilizer increases, and if it exceeds 10% by weight, the solid fertilizer becomes powdery and is not economical. In the present invention, either iron or aluminum is contained in 0.01 to 10%.
% By weight, but preferably contains iron and aluminum, and the weight ratio is from 1: 9 to 9:
1, more preferably from 4: 6 to 6: 4. The method for producing the solid fertilizer of the present invention is optional, and any conventionally known method may be used. For example, iron and / or aluminum may be added to the raw materials as a compound such as a salt or a complex. It is preferred to be manufactured by the method described in (I). This is to produce a fertilizer by chemically reacting the raw material, iron and / or aluminum in the fertilizer takes the form of a salt such as phosphate, which is an amorphous solid,
This is because the solid fertilizer has excellent effects of solidifying, reducing hygroscopicity, and disintegrating in water.
【0020】[0020]
【実施例】以下に実施例を示して本発明を更に具体的に
説明するが、本発明はその要旨を越えない限り、以下の
実施例に限定されるものではない。EXAMPLES The present invention will be described in more detail with reference to the following Examples, but it should not be construed that the present invention is limited to the following Examples without departing from the scope of the invention.
【0021】[実施例1]リン酸成分をP2 O5 として
44.1重量%、Alを0.29重量%、およびFeを
0.26重量%(何れも原子重量%換算)含有する湿式
燐酸161gに対し、55%尿素水溶液87gを添加
し、3〜10分間撹拌し、NPK成分比が17−44−
0のウレアフォスフェイト(UP)の結晶76gと母液
172gを得た。このスラリーを減圧濾過し、結晶と母
液を分離した。この結晶全量に対し、別系で同様の方法
で作成したUPの52%飽和溶液を159gを添加し、
新たなスラリーを作成した。このスラリーを撹拌しなが
ら、56%水酸化カリウム水溶液120gを5分かけて
滴入し、反応させ、水分を含んだゲル状物質約355g
を得た。この反応温度は最高温度で95℃であった。Example 1 A wet method containing 44.1% by weight of a phosphoric acid component as P 2 O 5 , 0.29% by weight of Al, and 0.26% by weight of Fe (all converted to atomic weight%) 87 g of a 55% aqueous urea solution was added to 161 g of phosphoric acid, and the mixture was stirred for 3 to 10 minutes.
Thus, 76 g of urea phosphate (UP) crystals and 172 g of mother liquor were obtained. The slurry was filtered under reduced pressure to separate crystals and mother liquor. To this total amount of crystals, 159 g of a 52% saturated solution of UP prepared in a similar manner in a separate system was added, and
A new slurry was made. While stirring the slurry, 120 g of a 56% aqueous solution of potassium hydroxide was dropped in over 5 minutes to cause a reaction, and about 355 g of a water-containing gel-like substance was reacted.
I got The reaction temperature was 95 ° C. at the highest temperature.
【0022】このゲル状物質を50℃、約8時間乾燥し
てNPK成分比が13−35−25で、Alを0.03
1重量%、Feを0.032重量%を含む固体肥料を得
た。乾燥後の固体肥料は196gであった。また同様に
ゲル状物質355gを得た後にこのゲル状物質に固体尿
素56gを混合・撹拌し、50℃、約8時間乾燥させた
ところ、NPK成分が20−27−19でAlを0.0
17重量%およびFeを0.018重量%を含む固体肥
料252gを得た。この固体肥料を23℃、80%RH
のインキュベーターに19時間放置し、吸湿による水分
増加量を測定した。その結果、本発明の固体肥料の重量
増加率は49%であり、吸湿による重量増加率は低かっ
た。The gel material is dried at 50 ° C. for about 8 hours, and the NPK component ratio is 13-35-25, and Al is 0.03%.
A solid fertilizer containing 1% by weight and 0.032% by weight of Fe was obtained. The solid fertilizer after drying was 196 g. Similarly, after obtaining 355 g of a gel-like substance, 56 g of solid urea was mixed and stirred with this gel-like substance, and dried at 50 ° C. for about 8 hours, whereby the NPK component was 20-27-19 and the Al content was 0.0%.
252 g of a solid fertilizer containing 17% by weight and 0.018% by weight of Fe were obtained. This solid fertilizer is heated at 23 ° C and 80% RH.
Was left in the incubator for 19 hours, and the amount of increase in water due to moisture absorption was measured. As a result, the rate of weight increase of the solid fertilizer of the present invention was 49%, and the rate of weight increase due to moisture absorption was low.
【0023】[実施例2]実施例1で使用した湿式燐酸
161gに紛状の固体尿素60gを添加し、撹拌し、N
PK成分比が17−44−0のUP132gと母液89
gを得た。このUPを減圧濾過し、UP全量に対し5.
6gの水を添加後、これを撹拌しながら56%水酸化カ
リウム水溶液56gを添加し、水分を含んだゲル状物質
約193.5gを得た。このゲル状物質に固体尿素56
gを混合・撹拌し、50℃、約8時間乾燥させたとこ
ろ、NPK成分比が22−27−16でAlを0.02
0重量%およびFeを0.021重量%を含む固体肥料
250gを得た。この固体肥料を実施例1と同様に吸湿
性試験を行ったところ、重量増加率は51%であった。Example 2 To 161 g of wet phosphoric acid used in Example 1 was added 60 g of powdery solid urea, and the mixture was stirred.
132 g of UP having a PK component ratio of 17-44-0 and mother liquor 89
g was obtained. This UP was filtered under reduced pressure, and 5.
After adding 6 g of water, 56 g of a 56% aqueous solution of potassium hydroxide was added with stirring to obtain about 193.5 g of a water-containing gel-like substance. Solid urea 56
g was mixed and stirred, and dried at 50 ° C. for about 8 hours. The NPK component ratio was 22-27-16, and Al was 0.02%.
250 g of a solid fertilizer containing 0% by weight and 0.021% by weight of Fe were obtained. When a moisture absorption test was performed on this solid fertilizer in the same manner as in Example 1, the weight increase rate was 51%.
【0024】[実施例3]実施例1同様に反応を行ない
水分を含んだゲル状物質355gを得て、これに固体尿
素74gと固体ジシアンジアミド10gを混合・撹拌
し、50℃、約8時間乾燥させたところ、NPK成分比
が23−24−17で、Alを0.014重量%および
Feを0.014重量%を含む固体肥料280gを得
た。この固体肥料を実施例1と同様に吸湿性試験を行っ
たところ、重量増加率は54%であった。Example 3 The reaction was carried out in the same manner as in Example 1 to obtain 355 g of a water-containing gel-like substance. 74 g of solid urea and 10 g of solid dicyandiamide were mixed and stirred, and dried at 50 ° C. for about 8 hours. As a result, 280 g of a solid fertilizer having an NPK component ratio of 23-24-17 and containing 0.014% by weight of Al and 0.014% by weight of Fe was obtained. When a moisture absorption test was performed on this solid fertilizer in the same manner as in Example 1, the weight increase rate was 54%.
【0025】[比較例1]実施例1と同様の方法で得ら
れたUPに水分を全く添加せずに固体水酸化カリウムを
同様に添加したところ、混合物は激しく反応し、アンモ
ニア臭がした。そして、得られた生成物は茶褐色の液状
であった。[Comparative Example 1] When solid potassium hydroxide was similarly added to the UP obtained in the same manner as in Example 1 without adding any water, the mixture reacted violently and smelled ammonia. And the obtained product was a brown liquid.
【0026】[比較例2]尿素粉末(710μmメッシ
ュ通過品)1gを用いて、実施例1と同様に吸湿性試験
を行った。その結果、尿素の重量増加率は73%であっ
た。Comparative Example 2 A moisture absorption test was conducted in the same manner as in Example 1 using 1 g of urea powder (a product having passed through a 710 μm mesh). As a result, the weight increase rate of urea was 73%.
【0027】[比較例3]尿素21%、塩化カリウム2
8%を含有しNPK成分比が16−16−16の固体肥
料(710μmメッシュ通過品)1gを用いて、実施例
1と同様に吸湿性試験を行った。その結果、この固体肥
料の重量増加率は98%であった。これらの実施例、比
較例の結果を、以下の表1および2に纏めた。Comparative Example 3 21% urea, 2 potassium chloride
A moisture absorption test was carried out in the same manner as in Example 1 using 1 g of a solid fertilizer containing 8% and having an NPK component ratio of 16-16-16 (a product passed through a 710 μm mesh). As a result, the weight increase rate of this solid fertilizer was 98%. The results of these Examples and Comparative Examples are summarized in Tables 1 and 2 below.
【0028】[0028]
【表1】 [Table 1]
【0029】[0029]
【表2】 [Table 2]
【0030】*:NPK比はN- P2 O5-K2 O( 重量
%) で表示した。 表−1および2から明らかなように、本発明の肥料の製
造方法は、製造工程で原料の分解が生ずることなく、肥
料の成分として効率良く用いることが可能となり、且つ
製品の肥料も、固体で、NPK成分が60%以上と高い
ものが得られる。*: The NPK ratio was expressed as NP 2 O 5 -K 2 O (% by weight). As is clear from Tables 1 and 2, the method for producing a fertilizer of the present invention can be used efficiently as a component of a fertilizer without decomposition of raw materials in the production process, and the fertilizer of the product is also solid. Thus, a high NPK component of 60% or more can be obtained.
【0031】[実施例4]実施例1と同様にウレアホス
フェイトと水酸化カリウム水溶液を反応させ、得られた
ゲル状物質を50℃約8時間乾燥して得られた物質(N
PK成分比:13−35−25:Alが0.031重量
%、Feを0.032重量%含有。すなわち、各元素を
リン酸塩換算した場合の含有量は、それぞれ0.14重
量%、0.14重量%である)を30℃、70%RHの
デシケーターに800時間放置し、吸湿による水分増加
量を測定した。その結果、重量増加率は35.0%であ
った。Example 4 A urea phosphate was reacted with an aqueous solution of potassium hydroxide in the same manner as in Example 1, and the obtained gel was dried at 50 ° C. for about 8 hours to obtain a substance (N
PK component ratio: 13-35-25: 0.031% by weight of Al and 0.032% by weight of Fe. That is, the content of each element in terms of phosphate is 0.14% by weight and 0.14% by weight, respectively). The solution is left in a desiccator at 30 ° C. and 70% RH for 800 hours to increase the water content by moisture absorption. The amount was measured. As a result, the weight increase rate was 35.0%.
【0032】[実施例5]リン酸成分をP2 O5 として
71.0重量%含む燐酸水溶液に、AlPO4 を0.0
7重量%、およびFePO4 ・nH2 Oを0.07重量
%添加したもの(37g)に、固体尿素15gを添加し
3〜10分間撹拌し、次いで56%水酸化カリウム水溶
液を30gを3分かけて滴下、反応させ、ゲル状物質8
2gを得た。この物質を50℃、8時間乾燥し実施例4
と同様の吸湿性評価を実施したところ、重量増加率は4
2.7%であった。Example 5 AlPO 4 was added to a phosphoric acid aqueous solution containing 71.0% by weight of a phosphoric acid component as P 2 O 5 in an amount of 0.02%.
15 g of solid urea was added to a mixture (7 g) containing 7 wt% and 0.07 wt% of FePO 4 .nH 2 O, and the mixture was stirred for 3 to 10 minutes. Then, 30 g of a 56% aqueous potassium hydroxide solution was added for 3 minutes. The reaction was carried out by dropping the gel-like substance 8
2 g were obtained. This material was dried at 50 ° C. for 8 hours and dried in Example 4.
When the same hygroscopicity evaluation was performed, the weight increase rate was 4
2.7%.
【0033】[実施例6]実施例5と同様の燐酸にAl
PO4 を0.14重量%、およびFePO4 ・nH2 O
を0.14重量%添加したもの(37g)に、実施例5
と同様に固体尿素および水酸化カリウム水溶液を反応さ
せ、乾燥したものの吸湿性評価を実施したところ、重量
増加率は35.0%であった。Example 6 The same phosphoric acid as in Example 5 was added to Al
0.14% by weight of PO 4 and FePO 4 .nH 2 O
Was added to 0.14% by weight (37 g) of Example 5 and
In the same manner as in the above, solid urea and an aqueous solution of potassium hydroxide were reacted and dried, and the hygroscopicity was evaluated. As a result, the weight increase rate was 35.0%.
【0034】[実施例7]AlPO4 を0.28重量%
およびFePO4 ・nH2 Oを0.28重量とした以外
は実施例5と同様にしてゲル状物質を得て吸湿性評価を
実施したところ、重量増加率は38.2%であった。Example 7 0.28% by weight of AlPO 4
A gel-like substance was obtained in the same manner as in Example 5 except that the amount of FePO 4 .nH 2 O was changed to 0.28 and the hygroscopicity was evaluated. As a result, the weight increase rate was 38.2%.
【0035】[実施例8]AlPO4 を0.7重量%お
よびFePO4 ・nH2 Oを0.7重量%とした以外は
実施例5と同様にしてゲル状物質を得て吸湿性評価を実
施したところ、重量増加率は40.0%であった。Example 8 A gel-like substance was obtained in the same manner as in Example 5 except that AlPO 4 was 0.7% by weight and FePO 4 .nH 2 O was 0.7% by weight, and the hygroscopicity was evaluated. As a result, the rate of weight increase was 40.0%.
【0036】[実施例9]実施例5と同様の燐酸37g
に実施例5同様に固体尿素および水酸化カリウム水溶液
を反応させ乾燥したものに吸湿性評価を実施したとこ
ろ、重量増加率が46.0%であった。実施例4〜9か
ら明らかな様に、本発明の製造方法によって得られた肥
料、および本発明の肥料は耐吸湿性に優れ、特に鉄及び
/又はアルミニウムを含有することで、さらに優れた耐
吸湿性を示す。Example 9 37 g of phosphoric acid as in Example 5
In the same manner as in Example 5, solid urea and an aqueous solution of potassium hydroxide were reacted and dried to evaluate the hygroscopicity. As a result, the rate of weight increase was 46.0%. As is clear from Examples 4 to 9, the fertilizer obtained by the production method of the present invention and the fertilizer of the present invention are excellent in moisture absorption resistance, and in particular, by containing iron and / or aluminum, more excellent resistance. Shows hygroscopicity.
【0037】[0037]
【発明の効果】本発明の肥料成分の製造方法は、安価な
UPとカリウム化合物を水の存在下で反応させること
で、加圧や加温をせず、製造コストを抑えて、硫酸根等
の副成分を含まない高成分肥料を製造可能とした優れた
ものである。加えて、製造工程中において原料が分解す
ること無く、原料を有効に肥料成分として利用できる、
優れた製造方法である。さらには窒素成分を添加するこ
とで、窒素成分が20%以上とした、あるいは窒素の肥
効を調節した、NPK成分が50%以上の高い固体肥料
成分を製造することが出来るものである。そして本発明
の固体肥料は、特定量の鉄及び/又はアルミニウムを含
有することで、高度化成肥料でありながら固体化し、吸
湿性を低減し、且つ水中崩壊性に優れた固体肥料であ
る。According to the method for producing a fertilizer component of the present invention, by reacting an inexpensive UP with a potassium compound in the presence of water, the production cost can be reduced without pressurizing or heating, and the production of sulfates and the like can be suppressed. This makes it possible to produce a high-component fertilizer that does not contain sub-components. In addition, the raw material can be effectively used as a fertilizer component without the raw material being decomposed during the manufacturing process.
It is an excellent manufacturing method. Further, by adding a nitrogen component, it is possible to produce a solid fertilizer component having an NPK component of 50% or more, in which the nitrogen component is adjusted to 20% or more, or the fertilizing effect of nitrogen is adjusted. The solid fertilizer of the present invention is a solid fertilizer containing a specific amount of iron and / or aluminum, which is a highly chemical fertilizer while solidifying, reducing moisture absorption, and being excellent in disintegration in water.
Claims (15)
を水の存在下で反応させることを特徴とする肥料の製造
方法。1. A method for producing a fertilizer, comprising reacting a urea phosphate with a potassium compound in the presence of water.
ミニウムを0.01〜20重量%含有することを特徴と
する請求項1に記載の製造方法。2. The method according to claim 1, wherein the urea phosphate contains 0.01 to 20% by weight of iron and / or aluminum.
とを反応して得られたものであることを特徴とする請求
項1または2に記載の製造方法。3. The production method according to claim 1, wherein the urea phosphate is obtained by reacting wet phosphoric acid with urea.
請求項3に記載の製造方法。4. The method according to claim 3, wherein the urea is solid urea.
反応が湿式燐酸と尿素との反応混合物から濾別した固形
物と、カリウム化合物溶液との反応であり、該反応を、
以下の(1)乃至(3)のいずれかの方法によって行な
うことを特徴とする請求項1乃至4のいずれかに記載の
製造方法。 (1)湿式燐酸と尿素との反応混合物から濾別した固形
物の溶液と、固体カリウム化合物又はその溶液とを反応
させる。 (2)湿式燐酸と尿素との反応混合物から濾別した固形
物に、カリウム化合物溶液を添加し反応させる。 (3)湿式燐酸と尿素との反応混合物から濾別した固形
物を、カリウム化合物溶液に添加し反応させる。5. The reaction between a urea phosphate and a potassium compound is a reaction between a solid substance filtered from a reaction mixture of wet phosphoric acid and urea and a potassium compound solution,
The method according to any one of claims 1 to 4, wherein the method is performed by any one of the following methods (1) to (3). (1) A solution of a solid substance filtered from a reaction mixture of wet phosphoric acid and urea is reacted with a solid potassium compound or a solution thereof. (2) A potassium compound solution is added to and reacted with a solid that has been filtered from the reaction mixture of wet phosphoric acid and urea. (3) A solid substance filtered from a reaction mixture of wet phosphoric acid and urea is added to a potassium compound solution and reacted.
徴とする請求項5に記載の製造方法。6. The method according to claim 5, wherein the solid solution is in the form of a slurry.
比が、1:0.5〜1:1.5であることを特徴とする
請求項1乃至6のいずれかに記載の製造方法。7. The process according to claim 1, wherein the molar ratio of urea phosphate to potassium is 1: 0.5 to 1: 1.5.
である請求項1乃至7のいずれかに記載の製造方法。8. The water content in the reaction system is 0.5 to 60% by weight.
The method according to any one of claims 1 to 7, wherein
リウムアルコキシドおよびカリウム塩からなる群より選
ばれるものであることを特徴とする請求項1乃至8のい
ずれかに記載の製造方法。9. The method according to claim 1, wherein the potassium compound is selected from the group consisting of potassium hydroxide, potassium alkoxide and potassium salt.
法により得られた肥料に、更に窒素成分を加えることを
特徴とする肥料の製造方法。10. A method for producing a fertilizer, further comprising adding a nitrogen component to the fertilizer obtained by the method according to any one of claims 1 to 9.
たはグアニジンであることを特徴とする請求項10に記
載の製造方法。11. The method according to claim 10, wherein the nitrogen component is urea, dicyandiamide or guanidine.
って被覆することを特徴とする請求項10または11に
記載の製造方法。12. The method according to claim 10, wherein a nitrogen component is used as a core material, and the core material is coated with a fertilizer.
る請求項1乃至12のいずれかに記載の製造方法。13. The method according to claim 1, wherein the fertilizer is a solid fertilizer.
成分の合計が50重量%以上であり、鉄及び/又はアル
ミニウムを0.01〜10重量%含有する固体肥料。14. A solid fertilizer containing a nitrogen component, a phosphoric acid component and a potassium component in a total amount of 50% by weight or more and containing 0.01 to 10% by weight of iron and / or aluminum.
とを特徴とする請求項14記載の固体肥料。15. The solid fertilizer according to claim 14, wherein the total nitrogen component is 20% by weight or more.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000021269A JP2001031488A (en) | 1999-05-14 | 2000-01-31 | Production of fertilizer and solid fertilizer |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13380799 | 1999-05-14 | ||
JP11-133807 | 1999-05-14 | ||
JP2000021269A JP2001031488A (en) | 1999-05-14 | 2000-01-31 | Production of fertilizer and solid fertilizer |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2001031488A true JP2001031488A (en) | 2001-02-06 |
Family
ID=26468051
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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JP2000021269A Pending JP2001031488A (en) | 1999-05-14 | 2000-01-31 | Production of fertilizer and solid fertilizer |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102070358A (en) * | 2010-11-17 | 2011-05-25 | 中国海洋石油总公司 | Method for preparing round and granular potassic fertilizer by utilizing post precipitation salt of phosphoric acid |
CN101367682B (en) * | 2008-09-28 | 2011-06-15 | 中国海洋石油总公司 | Method for preparing complex fertilizer with mutual solution slip tubular reactor |
-
2000
- 2000-01-31 JP JP2000021269A patent/JP2001031488A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101367682B (en) * | 2008-09-28 | 2011-06-15 | 中国海洋石油总公司 | Method for preparing complex fertilizer with mutual solution slip tubular reactor |
CN102070358A (en) * | 2010-11-17 | 2011-05-25 | 中国海洋石油总公司 | Method for preparing round and granular potassic fertilizer by utilizing post precipitation salt of phosphoric acid |
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