JPH01294520A - Method for slaking naturally occurring light burned magnesia - Google Patents
Method for slaking naturally occurring light burned magnesiaInfo
- Publication number
- JPH01294520A JPH01294520A JP509988A JP509988A JPH01294520A JP H01294520 A JPH01294520 A JP H01294520A JP 509988 A JP509988 A JP 509988A JP 509988 A JP509988 A JP 509988A JP H01294520 A JPH01294520 A JP H01294520A
- Authority
- JP
- Japan
- Prior art keywords
- light burned
- burned magnesia
- alkaline agent
- magnesia
- solution
- 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
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F5/00—Compounds of magnesium
- C01F5/14—Magnesium hydroxide
- C01F5/16—Magnesium hydroxide by treating magnesia, e.g. calcined dolomite, with water or solutions of salts not containing magnesium
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野1
本発明は、天然産のマグネサイトを焼成し、軽焼マグネ
シアとしたものを水と4I和反応させる方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field 1] The present invention relates to a method of calcining naturally produced magnesite to form lightly calcined magnesia and subjecting it to a 4I-reaction reaction with water.
[従来技術]
現在、一般的に工業用アルカリ剤としては、消石灰、苛
性ソーダ、水酸化マグネシウム等があるが、コストと物
理・化学的性質により、夫々使い分けられている。[Prior Art] Currently, slaked lime, caustic soda, magnesium hydroxide, etc. are commonly used as industrial alkali agents, and each is used depending on cost and physical/chemical properties.
[発明が解決しようとする問題点1
とりわけ、水酸化マグネシウムは、従米上り、海水中の
マグネジツムより多大のエネルギーと労力をかけて合成
されているのが実情である。[Problem to be Solved by the Invention 1] In particular, the reality is that magnesium hydroxide is synthesized using more energy and labor than magnesium in seawater.
本発明は、この水酸化マグネシウムを低コストで合成す
ることができ、且つ工業用アルカリ剤として市場に安価
に提供することができる、天然産軽焼マグネシアのi)
τ相方法を提供することを目的としている。The present invention is directed to i) naturally produced light calcined magnesia, which can synthesize this magnesium hydroxide at low cost and provide it to the market as an industrial alkali agent at low cost.
The purpose is to provide a τ-phase method.
[問題点を解決するための手段]
上記目的を達成するための本発明の構成は、天然産のマ
グネサイトを焼成した軽焼マグネシアを5〜30ミクロ
ンの超微粉に粉砕し、水に強アルカリ剤を添加し液のP
Hを11以上とし撹拌しながら上記野焼マグネシアを投
入し、混合液を100℃以上に加温することをその要旨
とするものである。[Means for Solving the Problems] The structure of the present invention to achieve the above object is to crush lightly calcined magnesia obtained by calcining naturally produced magnesite into an ultrafine powder of 5 to 30 microns, and add it to water with a strong alkali. Add the agent and increase the P of the liquid.
The gist of the method is to set H to 11 or more, add the above-mentioned open-fired magnesia while stirring, and heat the mixed liquid to 100° C. or more.
本発明方法により合成された水酸化マグネシウムは、高
活性のヒドロデル収水酸化マグネシウム又あるが、本出
願人はこの商品名を1サンヒドロマグ」と称しているの
で、以下他の水酸化マグネシウムと区別するため、便宜
上本発明方法により合成された水酸化マグネシウムをr
サンヒドロマグ」と言うことにする。Magnesium hydroxide synthesized by the method of the present invention is a highly active hydrodel-containing magnesium hydroxide, and the applicant calls this product ``1-sanhydromag'' to distinguish it from other magnesium hydroxides. Therefore, for convenience, magnesium hydroxide synthesized by the method of the present invention is
I'll call it "Sun Hydro Mag."
上記軽焼マグネシアは殆んどが中国、北鮮、インドにて
生産され輸入されている。原鉱はマグネサイ) (Mg
CO=)を主成分とし、不純物としてはへラフラン!
イ) (Ca2SiO+ + 1120)及びlIa量
ノア171.Xテライト(Mg2SiO+)を含んでい
る。Most of the light-burnt magnesia mentioned above is produced and imported in China, North Korea, and India. The raw ore is magnesai) (Mg
The main component is CO=), and the impurities are Herafuran!
b) (Ca2SiO+ + 1120) and lIa amount Noah 171. Contains X-telite (Mg2SiO+).
この原鉱を820℃府後で焼成することで、マグネサイ
トはべりクレース型MgOとなり、不純物のへラブフン
ゲイトはラルライトに変わり、フォルステライトは殆ん
ど尤のまま残っている。By calcining this raw ore at 820°C, magnesite becomes velclase-type MgO, the impurity herabhungite changes to rallite, and forsterite remains almost as it is.
二の軽焼マグネシアはMgOであるので、荷述の通りア
ルカリ剤として使用できるはずであり、特に排煙脱硫、
及び酸性排液の中和用のアルカリ剤として使用できれば
、海水より生産されている水酸性マグネジツム(以下“
海水マグとい))の生産コストの約半分で供給ができ、
大きな省コスト。Since the second light burnt magnesia is MgO, it should be able to be used as an alkaline agent as stated in the package, especially for flue gas desulfurization.
If it can be used as an alkaline agent for neutralizing acidic wastewater, hydroxymagnetium produced from seawater (hereinafter referred to as “
It can be supplied at about half the production cost of seawater mugs).
Big cost savings.
省エネルギーになるわけで、この点に着眼した多くの人
達が、過去間々の試験を重ねたが、結果はむしろ海水マ
グより反応が悪く、需要にまでは至らなかったのである
。This saves energy, and many people who have focused on this point have conducted repeated tests in the past, but the response was actually worse than that of seawater mugs, and there was no demand for them.
その理由は、単に軽焼マグネシアを水又は温水にて撹拌
させても消和がうまくできないためである。これは、軽
焼マグネシアのベリークレース型結晶構造(M[I原子
が6個の0原子に囲まれた密バ・ンキング構造)による
宿命的なものと解されていた。The reason for this is that light calcined magnesia cannot be slaked well even if it is simply stirred with water or hot water. This was considered to be a fateful result of the berryclase crystal structure (a dense banking structure in which an M[I atom is surrounded by six 0 atoms) of lightly burnt magnesia.
しかし、発明者は、ベリークレース型構造の解裂ハ液の
011−イオン濃度をアンモニア水又はカセイソーダ等
の強アルカリ剤を添加して高めることで6個のO原子は
7リーラジカル状の活性原子となることを見出したので
ある。However, the inventors discovered that by increasing the concentration of 011- ions in the cleavage solution having a berry crease structure by adding strong alkali agents such as aqueous ammonia or caustic soda, the 6 O atoms became active atoms in the form of 7-radicals. They found that.
この7リーラジカル原子を持つため反応性は極端に大き
くなり、海水マグの4〜5イ3の反応速度を持つに至っ
たのである。Because it has this 7-ary radical atom, its reactivity becomes extremely high, resulting in a reaction rate that is 4-5-3 that of seawater maggots.
サンヒドロマグの合成に際しては、ヒドロ化の反応速度
を上げるため、合成液温度を100 ”C以上とし、べ
+アークレース構造のM裂のため、#述の強アルカリ剤
を加え、液のPHを常温で測定して11以上とする。ま
た、反応時間は1時間以上とし充分撹拌し反応を終らせ
る。When synthesizing Sanhydromag, in order to increase the reaction rate of hydrolysis, the temperature of the synthesis liquid was set to 100"C or higher, and in order to create an M-cleavage of the base+arclace structure, a strong alkaline agent as mentioned in # was added, and the pH of the liquid was adjusted to room temperature. The reaction time should be 11 or more when measured with 1 hour or more, and the reaction should be completed with sufficient stirring.
[実施例1
鉄製の撹拌機付15+13反応槽に水91を入れ、撹拌
しながら強アルカリ剤を25Kg加え、充分溶解させる
。引続き、軽焼マグネシアを3600Kgを投入し混合
撹拌し、液温度を100℃以上に上げ、入チームを止め
る。[Example 1] 91 kg of water is placed in a 15+13 reaction tank equipped with an iron stirrer, and 25 kg of a strong alkaline agent is added while stirring, and the mixture is sufficiently dissolved. Subsequently, 3,600 kg of lightly burnt magnesia was added, mixed and stirred, and the liquid temperature was raised to 100°C or higher, and the addition of the mixture was stopped.
その状態で1時間以上撹拌し、消和反応を終らせる。Stir in this state for 1 hour or more to complete the slaked reaction.
反応が完全に終ったILW点で反応槽の中を7(χ検す
る。水がかなり蒸散し滅っているので、10m3(水中
サンヒドロマグ)になるように水を加えて濃度調整をし
てストレージタンクに移す。ストレージタンクより出荷
となる。At the ILW point where the reaction has completely finished, inspect the inside of the reaction tank.Since the water has evaporated considerably and disappeared, add water to adjust the concentration to 10m3 (underwater Sanhydromag) and store. Transfer to tank. Ship from storage tank.
サンヒドロマグは海水マグと異なr)極端に粘度が低い
のでがなり高い濃度スラリーとして運搬及び貯蔵ができ
る(実施例は40%濃度スラリーだが、50%濃度スラ
リーも可能)。Sanhydromag differs from seawater mug in that it has an extremely low viscosity, so it can be transported and stored as a highly concentrated slurry (the example is a 40% slurry, but a 50% slurry is also possible).
[発明の効果1
このサンヒドロマグは、排脱用アルカリ剤及び中和用ア
ルカリ剤としては前述のように非常な省コストと省エネ
に貢献するわけであるが、利点としてはそれだけでなく
、下記の、αもある。[Effect of the invention 1 This Sanhydromag contributes to significant cost and energy savings as an alkali agent for depletion and an alkali agent for neutralization, as mentioned above, but it also has the following advantages: There is also α.
1)海水マグ中のカルシウムは、Ca(Ofり2の形で
含まれているので、S02と反応して、亜硫酸カルシウ
ム(CaSOz)を形成してロック状の堆積物ができる
が、サンヒドロマグ中のCaOは、酸と反応しないラル
ライ) (Ca2SiJ)の形で含まれているので、亜
硫酸カルシウムは形成されず、従って、堆積物は発生し
ない。1) Calcium in seawater mags is contained in the form of Ca (Ofri2), so it reacts with S02 to form calcium sulfite (CaSOz) and form rock-like deposits. Since CaO is included in the form of Ralli) (Ca2SiJ), which does not react with acids, no calcium sulfite is formed and therefore no deposits occur.
2)サンヒドロマグは、設備を腐食させる要因となるC
gが含まれていなので、機器の損傷が少ない。2) Sanhydromag contains C, which causes corrosion of equipment.
Since it does not contain g, there is less damage to equipment.
特許出願人 株式会社 サンタレイ 手続補正書 昭和63年1り/&日 特許庁長官 小 川 邦 夫 殿C1 2、発明の名称 天然産軽焼マグネシアの消和方法 3、補正をする者 事件との関係 特許出願人 住 所 富山県富山市千原崎65 名称 株式会社サンタレイPatent applicant: Santaray Co., Ltd. Procedural amendment 19863 1/& day Commissioner of the Patent Office Kunio Kogawa C1 2. Name of the invention How to slake natural light burnt magnesia 3. Person who makes corrections Relationship to the case Patent applicant Address: 65 Chibarasaki, Toyama City, Toyama Prefecture Name Santaray Co., Ltd.
Claims (1)
5〜30ミクロンの超微粉に粉砕し、水に強アルカリ剤
を添加し、液のPHを11以上とし、撹拌しながら上記
軽焼マグネシアを投入し、混合液を100℃以上に加温
することを特徴とする天然産軽焼マグネシアの消和方法
。1) Lightly calcined magnesia made by calcining naturally produced magnesite is crushed into ultrafine powder of 5 to 30 microns, a strong alkaline agent is added to water, the pH of the liquid is adjusted to 11 or more, and the light calcined magnesia is mixed with stirring. A method for slaked naturally produced light-burnt magnesia, characterized by charging the mixture and heating the mixture to 100°C or higher.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP509988A JPH01294520A (en) | 1988-01-13 | 1988-01-13 | Method for slaking naturally occurring light burned magnesia |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP509988A JPH01294520A (en) | 1988-01-13 | 1988-01-13 | Method for slaking naturally occurring light burned magnesia |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH01294520A true JPH01294520A (en) | 1989-11-28 |
Family
ID=11601931
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP509988A Pending JPH01294520A (en) | 1988-01-13 | 1988-01-13 | Method for slaking naturally occurring light burned magnesia |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01294520A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0599085A1 (en) * | 1992-10-29 | 1994-06-01 | Daicel Abosisangyo Co., Ltd. | Method for the production of active magnesium hydroxide |
| WO1996002463A1 (en) * | 1994-07-15 | 1996-02-01 | Martin Marietta Magnesia Specialties Inc. | Stabilized, pressure-hydrated magnesium hydroxide slurry from burnt magnesite and process for its production |
| CN111943530A (en) * | 2020-08-20 | 2020-11-17 | 沈阳工业大学 | Preparation of light-burned magnesia and enrichment of carbon dioxide by self-circulating pyrolysis of flue gas |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6428214A (en) * | 1987-07-23 | 1989-01-30 | Nissan Eng Kk | Synthesis of active magnesium hydroxide |
-
1988
- 1988-01-13 JP JP509988A patent/JPH01294520A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6428214A (en) * | 1987-07-23 | 1989-01-30 | Nissan Eng Kk | Synthesis of active magnesium hydroxide |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0599085A1 (en) * | 1992-10-29 | 1994-06-01 | Daicel Abosisangyo Co., Ltd. | Method for the production of active magnesium hydroxide |
| WO1996002463A1 (en) * | 1994-07-15 | 1996-02-01 | Martin Marietta Magnesia Specialties Inc. | Stabilized, pressure-hydrated magnesium hydroxide slurry from burnt magnesite and process for its production |
| CN111943530A (en) * | 2020-08-20 | 2020-11-17 | 沈阳工业大学 | Preparation of light-burned magnesia and enrichment of carbon dioxide by self-circulating pyrolysis of flue gas |
| CN111943530B (en) * | 2020-08-20 | 2022-04-01 | 沈阳工业大学 | Method for preparing light-burned magnesia and enriching carbon dioxide by self-circulation pyrolysis of flue gas |
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