JPS5992984A - Manufacture of fused phosphate fertilizer - Google Patents

Manufacture of fused phosphate fertilizer

Info

Publication number
JPS5992984A
JPS5992984A JP20151882A JP20151882A JPS5992984A JP S5992984 A JPS5992984 A JP S5992984A JP 20151882 A JP20151882 A JP 20151882A JP 20151882 A JP20151882 A JP 20151882A JP S5992984 A JPS5992984 A JP S5992984A
Authority
JP
Japan
Prior art keywords
electric furnace
raw material
molten
molten phosphorus
heated
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
Application number
JP20151882A
Other languages
Japanese (ja)
Inventor
高橋 利喜二
飯島 穂
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.)
SEIBU KAGAKU KOGYO KK
Original Assignee
SEIBU KAGAKU KOGYO KK
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 SEIBU KAGAKU KOGYO KK filed Critical SEIBU KAGAKU KOGYO KK
Priority to JP20151882A priority Critical patent/JPS5992984A/en
Publication of JPS5992984A publication Critical patent/JPS5992984A/en
Pending legal-status Critical Current

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  • Fertilizers (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 この発明は、電気炉を用いる溶成リン側の製造方法の改
良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a method for producing molten phosphorus using an electric furnace.

従来から溶成リン側(以下熔リンと略称する)を製造す
る方法として、原料となるリン鉱石、蛇紋岩等を粒状に
粗砕して配合したのち、この配合原料を電気炉に投入し
て数千ボルトの高電圧を電極を介して印加することによ
って1300〜1500℃に加熱溶融し、得られた溶融
物を電気炉から流出せしめたのち水砕する方法が広く採
用されている。
Conventionally, the method for manufacturing molten phosphorus (hereinafter referred to as molten phosphorus) is to coarsely crush raw materials such as phosphate rock and serpentine into granules and mix them, and then feed this mixed raw material into an electric furnace. A widely used method is to apply a high voltage of several thousand volts through electrodes to melt the material by heating it to 1,300 to 1,500° C., to flow out the resulting molten material from an electric furnace, and then to pulverize it.

しかしながら、上記の方法によれば、原料の加熱溶融熱
源に高価な電力を使用するため、近年の電力価格高騰に
伴い製造コストに占める電力価格の割合が年々増大して
いるのが実情であり、電力使用量をできるだけ低減して
省エネルギー化を図ることができる方法の出現が望まれ
るところである。
However, according to the above method, since expensive electricity is used as a heat source for heating and melting the raw materials, the reality is that the proportion of electricity prices in manufacturing costs is increasing year by year due to the recent rise in electricity prices. There is a desire for a method that can reduce power consumption as much as possible and save energy.

また、熔リン原料を電気炉へ投入する前に通常は原料を
70〜80℃で乾燥するが、それでも水分を約2〜3%
含有しており、かような状態で電気炉に投入して加熱す
ると、生成する水蒸気によって炉内の溶融物がしばしば
沸騰する現象がみられる。この沸騰現象は安全面で問題
となるだけでなく、熱の損失という観点で好ましくない
In addition, the molten phosphorus raw material is usually dried at 70 to 80 degrees Celsius before being put into the electric furnace, but even then the moisture content is about 2 to 3%.
When placed in an electric furnace and heated in such a state, the molten material in the furnace often boils due to the generated water vapor. This boiling phenomenon not only poses a safety problem, but is also undesirable from the standpoint of heat loss.

この発明は、上述したような従来法における欠点を解消
し、原料の電気炉内での加熱溶融時の電力使用量を低減
して省エネルギーを図ることができ、しかも炉内溶融物
の沸騰現象を防止できる改良された熔リンの製造方法を
提供することを目的になされたものであって、その要旨
とするところは、熔リン原料を少なくとも300℃以上
に予備加熱したのち電気炉に投入することを特徴とする
ものである。
This invention eliminates the drawbacks of the conventional method as described above, reduces the power consumption when melting raw materials in an electric furnace, and saves energy. This was done with the purpose of providing an improved method for producing phosphorus that can prevent the occurrence of molten phosphorus, and its gist is to preheat the molten phosphorus raw material to at least 300°C or higher before charging it into an electric furnace. It is characterized by:

この発明の方法によれば、電気炉に原料を投入する前に
、比較的安価な熱源を用いて原料を予め少なくとも30
0℃に予備加熱でき、高価な電力を熱源として用いる電
気炉内では300℃から1300〜1500℃の溶融温
度まで加熱すればよいから、常温の原料を溶融温度まで
電気炉内で加゛熱する従来方法に比較して、熱源コスト
を大幅に低減させることができる。さらに、電気炉に投
入する原料は絶乾状態となっているから、電気炉内での
水蒸気発生に起因する沸騰現象も防止できる。
According to the method of the present invention, before the raw materials are introduced into the electric furnace, the raw materials are heated to at least 30% by using a relatively inexpensive heat source.
In an electric furnace that can be preheated to 0°C and uses expensive electricity as a heat source, it is sufficient to heat from 300°C to a melting temperature of 1300 to 1500°C, so raw materials at room temperature can be heated to the melting temperature in an electric furnace. Compared to conventional methods, heat source costs can be significantly reduced. Furthermore, since the raw materials fed into the electric furnace are in an absolutely dry state, boiling phenomena caused by water vapor generation within the electric furnace can be prevented.

なお、原料の予備加熱温度を高温にする程、電気炉にあ
(プる電ツノ使用量を低減できるが、それに伴い予備加
熱装置として耐熱性の高価な装置が必要となる。電気炉
にお(する電力使用向の実質的低減効果が得られ、しか
も特に耐熱性の高い高価な装置を使用しなくてもよいと
いう観点から、この発明にあける予備加熱温度は少なく
とも300°C以上、好ましくは400〜450°Cと
なる。一方、700℃以上の高温に予備加熱する場合に
は、耐熱性の予備加熱装置が必要となるだけでなく、原
料も熱分解してガスを発生するため好ましくない。
Note that the higher the preheating temperature of the raw materials is, the lower the amount of electric horns used in the electric furnace can be. (The preheating temperature in this invention is at least 300°C or higher, preferably at least 300°C, from the viewpoint of obtaining a substantial reduction effect in power consumption and not requiring the use of particularly heat-resistant and expensive equipment.) 400 to 450°C.On the other hand, when preheating to a high temperature of 700°C or higher, not only is a heat-resistant preheating device required, but the raw material also thermally decomposes and generates gas, which is undesirable. .

以下に添付図面に示ず好ましい実施例−を参照してこの
発明を詳述する。
The invention will now be described in detail with reference to preferred embodiments not shown in the accompanying drawings.

図示の好ましい実施例においては、熔リン原料の予備加
熱を古タイヤ等の有機廃棄物の乾留により発生する乾留
ガスの燃焼熱を用いて行なっている。すなわら、乾留装
置1内で古タイヤの加熱分解により生成した乾留ガスを
燃焼室2へ導き、助燃バーナー3により燃焼せしめて熱
風を発生させる。この熱風は熱風送m 機4により予備
加熱室5へ導かれる。
In the preferred embodiment shown, the molten raw material is preheated using the combustion heat of carbonization gas generated by carbonization of organic waste such as old tires. That is, carbonization gas generated by thermal decomposition of old tires in the carbonization apparatus 1 is guided to the combustion chamber 2 and combusted by the auxiliary burner 3 to generate hot air. This hot air is guided to a preheating chamber 5 by a hot air blower 4.

一方、熔リン原料は定量されてホッパー6から予備加熱
室5へ導入され、熱風により予備加熱される。予備加熱
室の構造としては、バンド乾燥装置、回転乾燥装置、流
動乾燥装置など種々のタイプの加熱乾燥装置が採用でき
るが、図示の好ましい実施例ではバンドコンベア7を具
備した加熱装置を用いている。
On the other hand, the molten raw material is metered and introduced from the hopper 6 into the preheating chamber 5, where it is preheated with hot air. As the structure of the preheating chamber, various types of heating drying devices such as a band drying device, a rotary drying device, and a fluidized drying device can be adopted, but in the preferred embodiment illustrated, a heating device equipped with a band conveyor 7 is used. .

予備加熱室5にて少なくとも300℃以上の品温になる
まで加熱された原料は、従来慣用されている電気炉8へ
投入され、電極9により加熱溶融され、溶融物はタップ
孔10から取出され、水噴射ノズル11からの水で急冷
破砕することによりガラス状の熔リン製品を得ることが
できる。
The raw material heated to a temperature of at least 300° C. in the preheating chamber 5 is put into a conventionally used electric furnace 8, heated and melted by an electrode 9, and the molten material is taken out from a tap hole 10. A glass-like molten product can be obtained by quenching and crushing with water from the water injection nozzle 11.

原料処理能力11000k Hの小型開放試験電気炉を
用いて行なった実験例を以下に挙げてこの発明の詳細な
説明する。
The present invention will be described in detail below with reference to an experimental example conducted using a small open test electric furnace having a raw material processing capacity of 11,000 kH.

図示した如き古タイヤ乾留装置1を用いて古タイヤ31
 )tgを乾留し、生成する乾留ガスを燃焼室2で燃焼
せしめて得られた熱風により、熔リン原料を予備加熱室
5内で420〜4GO’C(平均440℃)に加熱した
のち電気炉へ投入し、1300〜1500℃の溶融温度
まで加熱、溶融後、水冷して熔リン製品を製造した。こ
の場合の電気炉内での電力使用量は現状の25%減(製
品トン当り)であった。また、電気炉内で440℃の原
料を溶融温度まで昇温しで原料を加熱溶融するのに要す
る時間は約140分であり、この間、電気炉内での沸騰
現象は小規模なもの1回のみしか認められなかった。
The old tire 31 is heated using the old tire carbonization device 1 as shown in the figure.
) tg and the resulting carbonized gas is combusted in the combustion chamber 2. Using the hot air obtained, the molten phosphorus raw material is heated to 420 to 4 GO'C (average 440°C) in the preheating chamber 5, and then heated to an electric furnace. The mixture was heated to a melting temperature of 1,300 to 1,500°C, melted, and then cooled with water to produce a molten phosphorus product. In this case, the amount of electricity used in the electric furnace was 25% less than the current amount (per ton of product). In addition, it takes approximately 140 minutes to heat and melt raw materials at 440°C in an electric furnace to the melting temperature, and during this time, there is only one small-scale boiling phenomenon in the electric furnace. only was recognized.

一方、比較のため、従来と同様にして原料(品温17℃
)を予備加熱することなくそのまま電気炉へ投入し、1
300〜1500℃の溶融温度まで加熱溶融したのち水
冷して熔リン製品を製造した。この場合の電気炉での電
力使用量は1000KWH/製品トン(開放型試験炉の
ため放熱ロスを含む)であった。また、電気炉内で17
℃の原料を溶融温度まで昇温して原料を加熱溶融するの
に要する時間は約200分であり、この間、電気炉内で
の沸騰現象は大規模なもの1回、中規模なもの1回、小
規模なもの3回が認められた。
On the other hand, for comparison, raw materials (product temperature 17℃) were prepared in the same way as before.
) was put into the electric furnace as it was without preheating, and 1
After heating and melting to a melting temperature of 300 to 1,500°C, the mixture was cooled with water to produce a molten phosphorus product. The electric power consumption in the electric furnace in this case was 1000 KWH/ton of product (including heat radiation loss due to the open test furnace). In addition, 17
It takes about 200 minutes to heat the raw material at ℃ to the melting temperature and heat and melt the raw material, and during this time, there are one large-scale boiling event and one medium-sized boiling phenomenon in the electric furnace. , three small-scale cases were recognized.

上述したところかられかるようにこの発明の方法によれ
ば、原料を予備加熱せずに電気炉へ投入する従来方法に
比較して、熱源コストを大幅に減少できるだけでな(、
電気炉内での水蒸気発生に起因する沸騰現象の発生も効
果的に防止することができる。沸i規象光生時には安全
のために従来は電極への電圧印加を15〜20分間停止
していたが、沸騰現象の発生を防止できるこの発明方法
においてはかような電圧印加停止を解消できる。
As can be seen from the above, according to the method of the present invention, compared to the conventional method in which raw materials are charged into an electric furnace without preheating, it is possible to not only significantly reduce the cost of the heat source (
It is also possible to effectively prevent the occurrence of boiling phenomena caused by water vapor generation within the electric furnace. Conventionally, voltage application to the electrodes has been stopped for 15 to 20 minutes during boiling-state photogeneration for safety reasons, but this method of the present invention, which can prevent the occurrence of boiling phenomena, eliminates such stoppage of voltage application.

さらに、従来方法と較べてこの発明方法によれば、予め
原料を予備加熱しであるから電気炉内で溶融するに要す
る時間を約25〜30%短縮でき、このため電気炉1基
当りの生産能力を著しく向上させることができる。
Furthermore, compared to the conventional method, according to the method of the present invention, since the raw materials are preheated in advance, the time required for melting in the electric furnace can be reduced by about 25 to 30%, and therefore the production per electric furnace can be reduced by about 25 to 30%. ability can be significantly improved.

また、この発明方法を実施する場合、予備加熱した原料
を一度に多量に電気炉内に投入すると炉上部では原料湿
度が低下してしまうため、原料を少量宛炉内へ投入して
原料湿度が低下しないうちに溶融し、溶融物を連続タッ
プする方式を採用することが望ましい。かような連続タ
ップ方式を採用すると、炉内の溶融物滞留量は少なくな
るため、炉壁や電極ホルダーの損傷を低減でき、これら
の補修作業も少なくて済む。
In addition, when carrying out the method of this invention, if a large amount of preheated raw material is put into the electric furnace at once, the raw material humidity will drop in the upper part of the furnace. It is desirable to adopt a method in which the melt is melted before it decreases and the melt is continuously tapped. When such a continuous tap method is adopted, the amount of molten material retained in the furnace is reduced, so damage to the furnace wall and electrode holder can be reduced, and repair work for these can be reduced.

【図面の簡単な説明】[Brief explanation of drawings]

添付図面はこの発明の好ましい実施例を示寸説明図であ
る。 1・・・古タイヤ乾留装置、2・・・乾留ガス燃焼室、
5・・・予備加熱室、6・・・原料ホッパー、8・・・
電気炉。
The accompanying drawings are dimensional illustrations of preferred embodiments of the invention. 1... Old tire carbonization device, 2... Carbonization gas combustion chamber,
5... Preheating chamber, 6... Raw material hopper, 8...
Electric furnace.

Claims (1)

【特許請求の範囲】 1、リン鉱石および蛇紋岩からなる溶成リン側原料を電
気炉に投入し1300〜1500℃に加熱溶融したのち
水砕することからなる溶成リン側の製造方法において、
前記溶成リン側原料を少なくとも300°C以上に予備
加熱したのち電気炉に投入することを特徴とする溶成リ
ン側の製造方法。 2、前記予係′1加熱を有機廃棄物の乾留によりjqら
れる乾留ガスの燃焼熱を用いて行なう特許請求の範囲第
1項記載の方法。
[Claims] 1. A method for producing molten phosphorus, which comprises charging a molten phosphorus raw material consisting of phosphate rock and serpentinite into an electric furnace, heating and melting it at 1300 to 1500°C, and then crushing it with water.
A method for producing a molten phosphorus side material, characterized in that the molten phosphorus side raw material is preheated to at least 300°C or higher and then charged into an electric furnace. 2. The method according to claim 1, wherein the preheater '1 is heated using combustion heat of carbonization gas produced by carbonization of organic waste.
JP20151882A 1982-11-17 1982-11-17 Manufacture of fused phosphate fertilizer Pending JPS5992984A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20151882A JPS5992984A (en) 1982-11-17 1982-11-17 Manufacture of fused phosphate fertilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20151882A JPS5992984A (en) 1982-11-17 1982-11-17 Manufacture of fused phosphate fertilizer

Publications (1)

Publication Number Publication Date
JPS5992984A true JPS5992984A (en) 1984-05-29

Family

ID=16442369

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20151882A Pending JPS5992984A (en) 1982-11-17 1982-11-17 Manufacture of fused phosphate fertilizer

Country Status (1)

Country Link
JP (1) JPS5992984A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010024091A (en) * 2008-07-18 2010-02-04 Hitachi Zosen Corp Method for manufacturing phosphate fertiliser, and phosphate fertiliser

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010024091A (en) * 2008-07-18 2010-02-04 Hitachi Zosen Corp Method for manufacturing phosphate fertiliser, and phosphate fertiliser

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