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JPS59474B2 - Kankousei karihiriyou no seizouhouhou - Google Patents
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JPS59474B2 - Kankousei karihiriyou no seizouhouhou - Google Patents

Kankousei karihiriyou no seizouhouhou

Info

Publication number
JPS59474B2
JPS59474B2 JP1363574A JP1363574A JPS59474B2 JP S59474 B2 JPS59474 B2 JP S59474B2 JP 1363574 A JP1363574 A JP 1363574A JP 1363574 A JP1363574 A JP 1363574A JP S59474 B2 JPS59474 B2 JP S59474B2
Authority
JP
Japan
Prior art keywords
potash
potassium
compound
slow
release
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
JP1363574A
Other languages
Japanese (ja)
Other versions
JPS50105459A (en
Inventor
勝生 江口
勝朗 枡永
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.)
Ube Corp
Original Assignee
Ube Industries 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 Ube Industries Ltd filed Critical Ube Industries Ltd
Priority to JP1363574A priority Critical patent/JPS59474B2/en
Publication of JPS50105459A publication Critical patent/JPS50105459A/ja
Publication of JPS59474B2 publication Critical patent/JPS59474B2/en
Expired legal-status Critical Current

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  • Fertilizers (AREA)

Description

【発明の詳細な説明】 本発明は、カリ含有鉱物からり溶性のに20・Al2O
3・2 S + 02を主成分とする緩効性カリ肥料を
製造する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides 20.Al2O which is soluble in potassium-containing minerals.
This invention relates to a method for producing a slow-release potash fertilizer containing 3.2 S+02 as a main component.

カリ含有鉱物の主成分は、K2O・Al2O3・6 S
io 2であり、これを処理して得られるに20・A
l2O3・2 S t 02は水に不溶でしかもり溶性
であるため、これを緩効性のカリ肥料として用いること
は知られている。
The main component of potassium-containing minerals is K2O・Al2O3・6S
io 2, and the result obtained by processing this is 20・A
Since 12O3.2 S t 02 is insoluble in water but only slightly soluble, it is known to be used as a slow-release potash fertilizer.

その処理方法としては、カリ含有鉱物にカリ化合物を混
合し焼成する乾式方法(例えば、特公昭43−7816
)、あるいはカリ含有鉱物にカリ化合物の水溶液を混合
し、加熱・加圧処理する湿式方法(例えば、特公昭27
−4962号)の2つの方法が考えられている。
As a treatment method, a dry method in which a potash compound is mixed with a potash-containing mineral and fired (for example,
), or a wet method in which a potash-containing mineral is mixed with an aqueous solution of a potash compound and treated with heat and pressure (for example,
-4962) are being considered.

しかし両者には一長一短があり、どちらが経済的に有利
な方法であるかは一種に言及できないが、湿式方法は乾
式方法に比べて次の利点を有している。
However, both methods have their advantages and disadvantages, and it is difficult to say which method is more economically advantageous; however, the wet method has the following advantages over the dry method.

(1)反応温度が低いので所要熱量が少なくてすむ。(1) Since the reaction temperature is low, the amount of heat required is small.

(2)反応が均一に行なわれ易い。(2) It is easy to carry out the reaction uniformly.

(3)反応生成物の取り出しが容易である。(3) It is easy to take out the reaction product.

(4)高温焼成に伴うガスの発生による公害の心配がな
い。
(4) There is no need to worry about pollution caused by gas generated during high-temperature firing.

ところで従来提案されている湿式方法では、り溶性カリ
の約2倍量の水溶性カリが副生ずるため、その収率が極
めて低いという欠点を有しているばかりか、次の諸欠点
も有している。
By the way, the conventionally proposed wet method not only has the disadvantage of an extremely low yield since approximately twice the amount of water-soluble potash is produced as a by-product, but also has the following disadvantages: ing.

(1)多量のに20・n S t 02が副生じ、これ
がゲル伏となりろ過・水洗が極めて困難である。
(1) A large amount of 20·n S t 02 is produced as a by-product, and this forms a gelatinous substance, making it extremely difficult to filter and wash with water.

またろ過性を向上させるために多量の水を用いれば、カ
リ化合物の回収のための濃縮に莫大な熱量を必要とする
ことになる。
Furthermore, if a large amount of water is used to improve filterability, a huge amount of heat will be required for concentration to recover potassium compounds.

(2)過剰に用いたカリ化合物あるいは副生ずるカリ化
合物の回収が困難である。
(2) It is difficult to recover the potassium compound used in excess or the potassium compound produced as a by-product.

例えば副生じた水溶性カリ化合物を回収して再利用する
場合にハ、石灰あるいはドロマイトなどを添加し向性カ
リ溶液とする工程が必要である。
For example, when recovering and reusing by-product water-soluble potash compounds, it is necessary to add lime or dolomite to form a tropic potash solution.

そこで本発明者らは、従来提案されている湿式方法によ
る緩効性カリ肥料の製造方法に比べて、さらにすぐれた
方法を見い出すことを目的として種々鋭意研究を行った
Therefore, the present inventors conducted various studies with the aim of finding a method that is even better than the conventionally proposed method for producing slow-release potash fertilizer using a wet method.

その結果、カリ含有鉱物の粉砕物にカリ化合物の水溶液
とアルミニウム化合物とを混合し、ついでこれを加熱・
加圧処理した後、り溶性カリ化合物を分離収得すれば、
従来法の有していた諸欠点を全て改善することができ、
極めて経済的にカリ含有鉱物からに20・Al2O3・
2SiO2を主成分とする緩効性カリ肥料を製造するこ
とができることを見い出し、本発明を完成した。
As a result, an aqueous solution of a potash compound and an aluminum compound were mixed with the crushed material of the potash-containing mineral, which was then heated and heated.
If the soluble potassium compound is separated and obtained after pressure treatment,
All the drawbacks of conventional methods can be improved,
extremely economically from potash-containing minerals.
The present invention was completed by discovering that it is possible to produce a slow-release potash fertilizer containing 2SiO2 as a main component.

本発明において使用するカリ含有鉱物としては、カリ長
石、カリ石英粗面岩、絹雲母、蛭石、電気石、海緑石、
鉄みょうばん石などカリを含有している鉱物ならいずれ
も有効であり、これらを100インチメツシュ全通程度
に粉砕して用いるのがよい。
Potassium-containing minerals used in the present invention include potassium feldspar, potassium quartz trachyte, sericite, vermiculite, tourmaline, glauconite,
Any mineral containing potash such as iron alum stone is effective, and it is preferable to use these by crushing them into a 100-inch mesh.

またカリ化合物の水溶液としては、K2CO3゜KOH
などの水溶液が、さらにアルミニウム化合物としてはA
A’(OH)s 、 A 13203などが挙げられる
In addition, as an aqueous solution of potassium compound, K2CO3゜KOH
Aqueous solutions such as A
Examples include A'(OH)s, A 13203, and the like.

これらの混合割合は、得られる緩効性カリ肥料の収率、
あるいはそのろ過性などからみて、K2O15iO2(
モル比)が0.6〜1.0、Al2O3/ S i02
Cモル比)が0.4〜0.6になるように、カリ含有
鉱物の粉砕物に対してカリ化合物の水溶液とアルミニウ
ム化合物とを混合するのが好ましし)。
These mixing ratios determine the yield of slow-release potash fertilizer,
Or, considering its filterability etc., K2O15iO2(
molar ratio) is 0.6 to 1.0, Al2O3/Si02
It is preferable to mix an aqueous solution of a potash compound and an aluminum compound with respect to the ground material of a potash-containing mineral so that the C molar ratio) is 0.4 to 0.6).

つぎにこの混合物を150〜350℃の温度で5〜15
0kg/fflの圧力で1〜24時間加熱・加圧処理し
た後、冷却しろ過・水洗することによって、り溶性のに
20・Al2O3・2SiO2を主成分とする緩効性カ
リ肥料を収得する。
Next, this mixture is heated for 5 to 15 minutes at a temperature of 150 to 350°C.
After heating and pressurizing at a pressure of 0 kg/ffl for 1 to 24 hours, cooling, filtering, and washing with water, a slow-release potash fertilizer containing 20.Al2O3.2SiO2 as a main component is obtained.

本発明では、カリ含有鉱物にカリ化合物の水溶液の他に
アルミニウム化合物をあらかじめ混合しておくので従来
法においては加熱・加圧処理工程で副生ずる水溶性のカ
リ化合物(K2O・n5i02)啼*が、生成しないた
め、従来法に比べて極めて高収率(はとんど100%に
近い収率である)で緩効性カリ肥料を製造することがで
きる。
In the present invention, in addition to an aqueous solution of a potash compound, an aluminum compound is mixed in advance with the potash-containing mineral, so that water-soluble potash compounds (K2O・n5i02)*, which are produced as by-products in the heat and pressure treatment process in the conventional method, are eliminated. , is not produced, it is possible to produce slow-release potassium fertilizer at an extremely high yield (yield almost 100%) compared to conventional methods.

また水溶性のカリ化合物が加熱処理工程でほとんど副生
しないことにより、従来法の有していた諸欠点を全て改
善することができる。
In addition, since almost no water-soluble potassium compound is produced as a by-product during the heat treatment process, all the drawbacks of conventional methods can be overcome.

すなわち、生成物のろ過・水洗が極めて容易であり、ま
た過剰に用いたカリ化合物の回収も容易である。
That is, it is extremely easy to filter and wash the product with water, and it is also easy to recover the potassium compound used in excess.

このように本発明は、従来法に比べて極めてすぐれた新
規な緩効性カリ肥料の製造方法である。
As described above, the present invention is a novel method for producing slow-release potash fertilizer that is extremely superior to conventional methods.

次に本発明の実施例および比較例を挙げて、具体的に説
明する。
Next, examples of the present invention and comparative examples will be given to specifically explain the present invention.

なお各側で製造した緩効性カリ肥料の性状を第2表に示
した。
Table 2 shows the properties of the slow-release potassium fertilizers manufactured by each side.

また各側で用いたカリ含有鉱物は、第1表に示した化学
組成を有する山口系産出のカリ長石および大分系産出の
カリ石英粗面岩の粉砕物(100インチメツシュ全通)
である。
The potassium-containing minerals used on each side were crushed potassium feldspar produced in the Yamaguchi region and potassium quartz trachyte produced in the Oita region (all 100-inch mesh) having the chemical composition shown in Table 1.
It is.

実施例 1 カリ長石の粉砕物946gに、65%KOHの水溶液を
1,000g(K2O15iO2(モル比)二〇、7〕
、および純度95%の粉状のAl(OH)3を509
、!li’ (1’J303/ S 1o2(モル比)
=0.5J混合し200℃の温度で12kg/crtt
の圧力で12時間オートクレーブ中でかくはんしながら
加熱・加圧処理を行った。
Example 1 1,000 g of a 65% KOH aqueous solution was added to 946 g of crushed potassium feldspar (K2O15iO2 (molar ratio) 20.7).
, and powdered Al(OH)3 with a purity of 95% at 509
,! li'(1'J303/S 1o2 (molar ratio)
= 0.5J mixed and 12kg/crtt at a temperature of 200℃
Heat and pressure treatment was carried out with stirring in an autoclave for 12 hours at a pressure of .

得られた生成物を冷却しろ過した後、水洗・乾燥し、り
溶性のに20・Al2O3・2 S io 2を主成分
とする緩効性カリ肥料を1581g得た。
The obtained product was cooled and filtered, washed with water, and dried to obtain 1581 g of a slow-release potash fertilizer containing 20.Al2O3.2 S io 2 as a main component.

実施例 2〜3 加熱・加圧の処理条件を280℃の温度で49kg/c
rrtの圧力で2時間(実施例2)、320℃の温度で
100kg/fflの圧力で1時間(実施例3)とした
他は実施例1と同様の方法によって実験を行い、緩効性
カリ肥料を、l、580g(実施例2)、1.581g
(実施例3)得た。
Examples 2-3 Heating and pressurizing treatment conditions: 49 kg/c at a temperature of 280°C
An experiment was conducted in the same manner as in Example 1, except that the temperature was 2 hours at a pressure of , l, 580g (Example 2), 1.581g
(Example 3) Obtained.

比較例 Al(OH)3を混合しなかった他は、実施例1と同様
の方法で実験を行い、緩効性カリ肥料を608g得た。
Comparative Example An experiment was conducted in the same manner as in Example 1, except that Al(OH)3 was not mixed, and 608 g of slow-release potassium fertilizer was obtained.

実施例 4 カリ長石の粉砕物845gに1.48%KOHの水溶液
を1,000 g(に2O/ S t 02 (モル比
)−〇、6バおよび純度95%の粉状のA7(OH)3
を597 g(A12C)3/ S t 02 (モル
比)=0.6J混合し、250℃の温度で30kg/i
の圧力で10時間オートクレーブ中でかくはんしながら
加熱・加圧処理を行った。
Example 4 1,000 g of a 1.48% KOH aqueous solution was added to 845 g of crushed potassium feldspar (2O/S t 02 (molar ratio) - 0, 6 bar and powdered A7 (OH) with a purity of 95%). 3
597 g (A12C)3/S t 02 (molar ratio) = 0.6 J and mixed at 30 kg/i at a temperature of 250°C.
Heat and pressure treatment was performed with stirring in an autoclave for 10 hours at a pressure of .

得られた生成物を冷却しろ過した後、これを水洗・乾燥
し、緩効性カリ肥料を1.413g得た。
After cooling and filtering the obtained product, it was washed with water and dried to obtain 1.413 g of slow-release potassium fertilizer.

実施例 5 カリ石英粗面岩の粉砕物637gに、60%に2CO3
の水溶液を1.000 g(に2O/ S i 02(
モル比)=0.7〕、および純度98%の粉状のAl2
O3を277 g(A40a / S 102 (モル
比)=0.5J混合し、250℃の温度で30kg/i
の圧力で5時間オートクレーブ中でかくはんしながら加
熱・加圧処理を行った。
Example 5 637g of crushed potassium quartz trachyte was added with 2CO3 to 60%.
1.000 g of an aqueous solution of 2O/S i 02(
molar ratio) = 0.7] and powdered Al2 with a purity of 98%.
Mix 277 g of O3 (A40a / S 102 (molar ratio) = 0.5 J, 30 kg/i at a temperature of 250 ° C.
Heat and pressure treatment was performed while stirring in an autoclave for 5 hours at a pressure of .

得られた生成物を冷却しろ過した後、これを水洗・乾燥
し、緩効性カリ肥料を1.13!l得た。
After cooling and filtering the obtained product, it was washed with water and dried, and a slow-release potassium fertilizer was added to the solution at a concentration of 1.13! I got it.

Claims (1)

【特許請求の範囲】[Claims] 1 カリ含有鉱物の粉砕物にカリ化合物の水溶液とアル
ミニウム化合物とを混合し、ついでこれを加熱・加圧処
理した後、り溶性カリ化合物を分離収得することを特徴
とする緩効性カリ肥料の製造方法。
1. Production of a slow-release potash fertilizer characterized by mixing an aqueous solution of a potash compound and an aluminum compound with a crushed product of potash-containing minerals, then subjecting the mixture to heat and pressure treatment, and then separating and obtaining a soluble potash compound. Method.
JP1363574A 1974-02-04 1974-02-04 Kankousei karihiriyou no seizouhouhou Expired JPS59474B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1363574A JPS59474B2 (en) 1974-02-04 1974-02-04 Kankousei karihiriyou no seizouhouhou

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1363574A JPS59474B2 (en) 1974-02-04 1974-02-04 Kankousei karihiriyou no seizouhouhou

Publications (2)

Publication Number Publication Date
JPS50105459A JPS50105459A (en) 1975-08-20
JPS59474B2 true JPS59474B2 (en) 1984-01-06

Family

ID=11838679

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1363574A Expired JPS59474B2 (en) 1974-02-04 1974-02-04 Kankousei karihiriyou no seizouhouhou

Country Status (1)

Country Link
JP (1) JPS59474B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5969418A (en) * 1982-10-14 1984-04-19 Takamura Suzuki Method for obtaining citric soluble potash fertilizer as well as white powder, deoxidizer, starting material for ceramic or the like from potash ore and lime, magnesia or the like
JP5727142B2 (en) * 2009-01-23 2015-06-03 株式会社 東北テクノアーチ Method for producing slow-acting fertilizer

Also Published As

Publication number Publication date
JPS50105459A (en) 1975-08-20

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