JP2005501791A5 - - Google Patents

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Publication number
JP2005501791A5
JP2005501791A5 JP2003524936A JP2003524936A JP2005501791A5 JP 2005501791 A5 JP2005501791 A5 JP 2005501791A5 JP 2003524936 A JP2003524936 A JP 2003524936A JP 2003524936 A JP2003524936 A JP 2003524936A JP 2005501791 A5 JP2005501791 A5 JP 2005501791A5
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JP
Japan
Prior art keywords
fluidized bed
metal halide
particles
halide particles
fluidized
Prior art date
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Application number
JP2003524936A
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Japanese (ja)
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JP2005501791A (en
JP4812253B2 (en
Filing date
Publication date
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Priority claimed from PCT/US2001/027160 external-priority patent/WO2003020663A1/en
Publication of JP2005501791A publication Critical patent/JP2005501791A/en
Publication of JP2005501791A5 publication Critical patent/JP2005501791A5/ja
Application granted granted Critical
Publication of JP4812253B2 publication Critical patent/JP4812253B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Claims (17)

ハロゲン化アルカリ金属とハロゲン化アルカリ土類金属とからなる群から選ばれるハロ
ゲン化金属粒子を対応する1種又は複数種の硫酸塩へ変換する方法であって、ハロゲン化
金属粒子を二酸化硫黄と水蒸気と空気とを含む流動気体と十分な速度で接触させてハロゲ
ン化金属粒子の流動床を形成させ、この流動床を約204℃(約400°F)から約87
1℃(約1600°F)の範囲の温度で十分な時間維持して、気体を生成させるとともに
、ハロゲン化金属粒子を対応する1種又は複数種の硫酸塩に変換させることを特徴とする
ハロゲン化金属粒子を硫酸塩へ変換する方法。
A method of converting metal halide particles selected from the group consisting of alkali metal halides and alkaline earth metal halides into one or more corresponding sulfates, wherein the metal halide particles are converted to sulfur dioxide and water vapor. And a fluidized gas comprising air and air at a sufficient rate to form a fluidized bed of metal halide particles, the fluidized bed being about 204 ° C (about 400 ° F) to about 87 ° C.
A halogen characterized by maintaining a temperature in the range of 1 ° C. (about 1600 ° F.) for a sufficient period of time to produce a gas and to convert the metal halide particles into the corresponding one or more sulfates. To convert metal halide particles into sulfate.
前記ハロゲン化金属粒子の1種又は複数種のハロゲン化物は、塩化物、フッ化物、臭化
物およびそれらの混合物からなる群から選ばれることを特徴とする請求項1記載の方法。
2. The method of claim 1, wherein the one or more halides of the metal halide particles are selected from the group consisting of chloride, fluoride, bromide, and mixtures thereof.
前記ハロゲン化金属粒子の1種又は複数種の金属は、カリウム、ナトリウム、カルシウ
ムおよびそれらの混合物からなる群から選ばれることを特徴とする請求項1記載の方法。
2. The method according to claim 1, wherein the one or more metals of the metal halide particles are selected from the group consisting of potassium, sodium, calcium and mixtures thereof.
前記流動床は約30cmから約1.2m(約12インチから4フィート)の範囲の深さ
を有することを特徴とする請求項1記載の方法。
The method of claim 1, wherein the fluidized bed has a depth in the range of about 30 cm to about 1.2 m (about 12 inches to 4 feet).
前記流動気体とハロゲン化金属粒子との接触を十分な時間維持して、前記流動床から出
る流動気体から実質的に全ての硫黄含有気体を除去することを特徴とする請求項4の方法
5. The method of claim 4, wherein contact between the flowing gas and the metal halide particles is maintained for a sufficient time to remove substantially all of the sulfur-containing gas from the flowing gas exiting the fluidized bed.
前記二酸化硫黄は元素硫黄を燃焼して製造したことを特徴とする請求項1記載の方法。   The method according to claim 1, wherein the sulfur dioxide is produced by burning elemental sulfur. 前記流動気体はSO3 を含むことを特徴とする請求項1の方法。 The method of claim 1, wherein the flowing gas comprises SO 3 . ハロゲン化アルカリ金属とハロゲン化アルカリ土類金属とからなる群から選ばれるハロ
ゲン化金属粒子を対応する1種又は複数種の硫酸塩へ変換する方法であって、二酸化硫黄
と水蒸気と空気とを含む流動気体をハロゲン化金属粒子に十分な速度で通過させてハロゲ
ン化金属粒子を流動させこの流動を維持することによって、一連の複数のハロゲン化金属
粒子流動床を形成し、一連の複数流動床の最後の流動床を出る流動気体は硫黄を実質的に
含まずかつ一連の複数流動床の最初の流動床を出る粒子はハロゲン化物を実質的に含まな
いようになるまで、一連の複数流動床おける一つの流動床から出る流動気体をもう一つの
流動床に通過させることを特徴とするハロゲン化金属粒子を硫酸塩へ変換する方法。
A method for converting metal halide particles selected from the group consisting of alkali metal halides and alkaline earth metal halides into one or more corresponding sulfates, comprising sulfur dioxide, water vapor and air By passing the flowing gas through the metal halide particles at a sufficient speed to flow and maintain the flow of metal halide particles, a series of metal halide particle fluidized beds are formed, The fluidized gas exiting the last fluidized bed is substantially free of sulfur and the particles exiting the first fluidized bed of the series of fluidized beds are substantially free of halide in a series of fluidized beds. A method for converting metal halide particles into sulfate, wherein a fluid gas exiting from one fluidized bed is passed through another fluidized bed.
前記粒子は一連の複数流動床における流動床から流動床へ移送されることを特徴とする
請求項8記載の方法。
The method of claim 8, wherein the particles are transferred from fluidized bed to fluidized bed in a series of multiple fluidized beds.
前記流動気体は、前記粒子の移送方向と対向する方向に流動させることを特徴とする請
求項9記載の方法。
The method according to claim 9, wherein the flowing gas is caused to flow in a direction opposite to a transfer direction of the particles.
前記ハロゲン化金属粒子の1種又は複数種のハロゲン化物は、塩化物、フッ化物、臭化
物およびそれらの混合物からなる群から選ばれ、前記ハロゲン化金属粒子の1種又は複数
種の金属は、カリウム、ナトリウム、カルシウムおよびそれらの混合物からなる群から選
ばれることを特徴とする請求項10記載の方法。
The one or more halides of the metal halide particles are selected from the group consisting of chlorides, fluorides, bromides and mixtures thereof, and the one or more metals of the metal halide particles are potassium 11. The method of claim 10, wherein the method is selected from the group consisting of sodium, calcium, and mixtures thereof.
各流動床は約30cmから約1.2m(約12インチから4フィート)の範囲の深さを
有することを特徴とする請求項11記載の方法。
The method of claim 11, wherein each fluidized bed has a depth in the range of about 30 cm to about 1.2 m (about 12 inches to 4 feet).
前記流動気体における二酸化硫黄は元素硫黄を燃焼して製造したことを特徴とする請求
項8記載の方法。
9. The method of claim 8, wherein the sulfur dioxide in the flowing gas is produced by burning elemental sulfur.
前記流動気体中の硫黄はSO3 を含むことを特徴とする請求項8記載の方法。 The sulfur in the flowing gas The method of claim 8, wherein the containing SO 3. 前記複数の流動床は単一の容器中に垂直に配列され、一つの流動床からの粒状物質がよ
り低い位置の流動床へと流下し、より低い位置の流動床から出る気体がより高い位置の流
動床を通って流れるようにしたことを特徴とする請求項8記載の方法。
The plurality of fluidized beds are arranged vertically in a single vessel so that particulate matter from one fluidized bed flows down to a lower fluidized bed and the gas exiting the lower fluidized bed is higher. 9. A process according to claim 8, wherein the process is made to flow through a fluidized bed.
前記複数の流動床が垂直に配列され、粒子は流動気体に対して対向するように流れ、ハ
ロゲン化物含有量の最も高い粒子は酸化硫黄含有量の最も低い気体と接触するようにした
ことを特徴とする請求項8記載の方法。
The plurality of fluidized beds are arranged vertically, the particles flow so as to face the flowing gas, and the particles having the highest halide content are in contact with the gas having the lowest sulfur oxide content. The method according to claim 8.
ハロゲン化物は塩化物であり、金属はカリウム又はカルシウムであることを特徴とする
請求項8記載の方法。
9. A method according to claim 8, wherein the halide is chloride and the metal is potassium or calcium.
JP2003524936A 2001-08-29 2001-08-29 Method for producing potassium sulfate fertilizer and other metal sulfates Expired - Fee Related JP4812253B2 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/US2001/027160 WO2003020663A1 (en) 1998-06-22 2001-08-29 A process for manufacturing potassium sulfate fertilizer and other metal sulfates

Publications (3)

Publication Number Publication Date
JP2005501791A JP2005501791A (en) 2005-01-20
JP2005501791A5 true JP2005501791A5 (en) 2005-12-22
JP4812253B2 JP4812253B2 (en) 2011-11-09

Family

ID=45044770

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2003524936A Expired - Fee Related JP4812253B2 (en) 2001-08-29 2001-08-29 Method for producing potassium sulfate fertilizer and other metal sulfates

Country Status (1)

Country Link
JP (1) JP4812253B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2020165974A1 (en) * 2019-02-13 2021-12-09 日揮グローバル株式会社 Sulfation roasting method

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5795825A (en) * 1980-12-08 1982-06-14 Asahi Chem Ind Co Ltd Manufacture of potassium sulfate
JPS58161917A (en) * 1982-03-19 1983-09-26 Onoda Kagaku Kogyo Kk Manufacture of potassium sulfate
JPS60180913A (en) * 1984-02-28 1985-09-14 Chisso Corp Method for neutralizing modified potassium sulfate by dry process
JPH05186216A (en) * 1990-04-10 1993-07-27 Mitsubishi Gas Chem Co Inc Production of potassium sulfate and hydrochloric acid
CA2284967A1 (en) * 1998-10-13 2000-04-13 Aristos Capital Corporation Method of formulating alkali earth salts

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