JPH10101331A - High reactivity slaked lime and its production - Google Patents

High reactivity slaked lime and its production

Info

Publication number
JPH10101331A
JPH10101331A JP27707696A JP27707696A JPH10101331A JP H10101331 A JPH10101331 A JP H10101331A JP 27707696 A JP27707696 A JP 27707696A JP 27707696 A JP27707696 A JP 27707696A JP H10101331 A JPH10101331 A JP H10101331A
Authority
JP
Japan
Prior art keywords
water
slaked lime
lime
amines
alcohols
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
JP27707696A
Other languages
Japanese (ja)
Inventor
Yoshikatsu Kawashima
好勝 河嶋
Tomio Oda
富雄 織田
Tsutomu Sawada
勉 澤田
Katsuhiko Amano
克彦 天野
Matsuzo Kada
松藏 加田
Koichi Miyayama
孝一 宮山
Norifumi Oukura
徳文 巨椋
Katsuhiko Hoshiyama
勝彦 星山
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.)
Omi Kogyo Co Ltd
Omi Mining Co Ltd
Original Assignee
Omi Kogyo Co Ltd
Omi Mining Co 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 Omi Kogyo Co Ltd, Omi Mining Co Ltd filed Critical Omi Kogyo Co Ltd
Priority to JP27707696A priority Critical patent/JPH10101331A/en
Publication of JPH10101331A publication Critical patent/JPH10101331A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To easily obtain high reactivity slaked lime having high reactivity with acidic gas in the conventional facilities by adding alcohols, amines or saccharides to powdery quick lime and bringing them into slaking reaction with water. SOLUTION: One or more kinds of alcohols, amines or saccharides are added to quick lime by 0.02-50wt.%, preferably 0.5-25wt.% of the amt. of the quick lime, they are mixed or the quick lime is coated with the additives and slaking water is added to produce the objective high reactivity slaked lime having a large specific surface area. In other way, the additives are dissolved in water to produce slaking water and quick lime is slaked with the slaking water. Water-soluble glycol and glycerol are preferably used as the alcohols. Water-soluble prim. to tert. amines are used as the amines. Sucrose and glucose are used as the saccharides.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は塵芥焼却炉の燃焼ガ
スなどの処理にあたり、酸性ガス等の除去を効率的に行
うために、反応性を高めた消石灰および反応性を高めた
消石灰を工業的に有利に製造する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for industrially removing slaked lime with enhanced reactivity and slaked lime with enhanced reactivity in order to efficiently remove acid gases and the like in the treatment of combustion gas and the like in a refuse incinerator. And a method for producing the same advantageously.

【0002】[0002]

【従来の技術】消石灰の製造方法には、大きく分けて湿
式消化方法と乾式消化方法があるが、工業的に消石灰を
粉末で得るためには、通常乾式消化方法が行われてい
る。
2. Description of the Related Art Slaked lime production methods are broadly classified into wet digestion and dry digestion. In order to obtain slaked lime as a powder in industry, a dry digestion method is generally used.

【0003】乾式消化方法を工業的に行うには、トップ
サイズを5mm程度またはそれ以下に破砕粉砕した生石灰
を原料供給装置により、加水装置を備えた消化機とよば
れる反応装置に供給し、加水攪拌を行い消化反応をさせ
る。この時粉粒状の生石灰は水と反応し消石灰となり粒
は崩壊する。消化反応を終えた消石灰は、粒と粉が混ざ
り合った状態であり、熟成機を経て分級機に供給され、
粗粉と細粉に分けられて、細粉は製品となる。
In order to carry out the dry digestion method industrially, quick lime obtained by crushing and pulverizing the top size to about 5 mm or less is supplied to a reactor called a digester equipped with a water supply device by a raw material supply device, and the water is added to the water. Stir to allow digestion reaction. At this time, the powdered and granular quicklime reacts with water and becomes slaked lime, and the grains collapse. The slaked lime that has finished the digestion reaction is in a state in which grains and powder are mixed, and is supplied to a classifier through an aging machine.
Fine powder is divided into coarse powder and fine powder.

【0004】この製造方法において、加えられる水は原
料の生石灰に対して、32〜70重量%である。この時
加えられた水は、生石灰との反応に消費され、余剰の水
は消化反応時の発熱により蒸発し、製品中には適度な水
分が残る。
In this production method, the amount of water to be added is 32 to 70% by weight based on quicklime as a raw material. The water added at this time is consumed in the reaction with quick lime, and the excess water evaporates due to the heat generated during the digestion reaction, and an appropriate amount of water remains in the product.

【0005】このような従来法で得られた消石灰は、J
IS Z 9001 に定められる消石灰特号あるいは
1号であり、その空気透過法によるブレーン値は10,
000〜20,000平方センチメートル/グラム、窒
素吸着法によるBET比表面積は10〜20平方メート
ル/グラムである。
The slaked lime obtained by such a conventional method is described in J.
It is slaked lime special number or 1 specified in ISZ9001, and its Blaine value by the air permeation method is 10,
000-20,000 square centimeters / gram, and BET specific surface area by nitrogen adsorption method is 10-20 square meters / gram.

【0006】酸性ガスとの反応性を高めるためには、比
表面積を大きくすればよいと言われている。従来の製造
方法で比表面積を大きくするには、分級点を小粒子径に
設定して分級することが考えられるが、この方法では製
品の歩留りが低下し、比表面積の増加も限られている。
It is said that the specific surface area should be increased in order to increase the reactivity with the acidic gas. In order to increase the specific surface area by the conventional manufacturing method, it is conceivable to classify the particles by setting the classification point to a small particle diameter, but this method reduces the product yield and increases the specific surface area. .

【0007】また、エタノール、メタノールを消化水に
混合して、生石灰を消化すると、高比表面積の消石灰が
得られることが知られており、特許公報平6−8194
においては、生石灰を、水と反応を遅延せしめる有機溶
剤とからなる消和液体に強力かつ均一に混合し高比表面
積の消石灰を得ることを提案している。この時の有機溶
剤はメタノール、エタノール、プロパノール、ブタノー
ルのようなアルコールならびにケトン、エーテルおよび
アルデヒドである。しかし、この方法においては、有機
溶剤は水に混合した状態で使用されており、その量は消
化水中の50〜70容量部必要となっている。また消化
過程において、加熱装置や脱ガス装置および複数の反応
容器等の特殊設備が必要となる。
[0007] It is known that slaked lime having a high specific surface area can be obtained by mixing ethanol and methanol with digested water to digest quicklime.
Proposes to obtain a slaked lime with a high specific surface area by mixing quicklime strongly and uniformly with a slaked liquid composed of water and an organic solvent that delays the reaction. Organic solvents at this time are alcohols such as methanol, ethanol, propanol and butanol, as well as ketones, ethers and aldehydes. However, in this method, the organic solvent is used in a state of being mixed with water, and the amount thereof is required to be 50 to 70 parts by volume in the digested water. In the digestion process, special equipment such as a heating device, a degassing device, and a plurality of reaction vessels is required.

【0008】また公開特許公報平5−193997にお
いては、メタノール及び/またはエタノールをアルコー
ル濃度が5〜60体積%になるように水と混和し更に界
面活性剤を加えた状態で生石灰と反応させることを提案
している。この場合もアルコールが生石灰に対して多く
の量が必要であり、アルコール回収搭などの特殊設備が
必要となる。
In Japanese Patent Laid-Open Publication No. 5-193997, methanol and / or ethanol are mixed with water so that the alcohol concentration becomes 5 to 60% by volume, and further reacted with quicklime with a surfactant added. Has been proposed. In this case, too, a large amount of alcohol is required for quicklime, and special equipment such as an alcohol recovery tower is required.

【0009】[0009]

【発明が解決しようとする課題】発明者等は、酸性ガス
との反応性の高い消石灰、つまり高比表面積の消石灰を
得るためには、従来の方法では加熱装置やアルコール回
収塔等の特殊設備が必要であることに着目し、加熱装置
やアルコール回収塔などの特殊設備を必要とせず、従来
からの消化設備で工業的に有利に製造することを課題と
した。
SUMMARY OF THE INVENTION In order to obtain slaked lime having high reactivity with acid gas, that is, slaked lime having a high specific surface area, the present inventors require special equipment such as a heating device and an alcohol recovery tower in a conventional method. It is an object of the present invention to industrially and advantageously use conventional digestion equipment without requiring special equipment such as a heating device and an alcohol recovery tower.

【0010】[0010]

【課題を解決するための手段】発明者等は、上記課題を
解決するために鋭意研究を重ねた結果、アルコール類、
アミン類、糖類の存在下で生石灰を消化反応させると比
表面積が大きい消石灰が得られることを見出し、かつ原
料生石灰を粉砕することにより、効率的にねらいとする
消石灰を得られることを見出した。本知見に基づいて、
本発明を完成するに至った。
Means for Solving the Problems The inventors have conducted intensive studies to solve the above problems, and as a result, have found that alcohols,
It has been found that slaked lime having a large specific surface area can be obtained when a quick lime is digested and reacted in the presence of amines and saccharides, and that slaked lime can be efficiently obtained by pulverizing raw lime. Based on this finding,
The present invention has been completed.

【0011】まずグリコール類、グリセリン類等の二価
および三価で水に可溶なアルコール類、第一級アミン
類、第二級アミン類および第三級アミン類で水に可溶な
アミン類、またはショ糖、ブドウ糖、果糖等の水に可溶
な糖類から選択された1種類または2種類以上の添加剤
は、生石灰に対して0.01〜50重量%好ましくは
0.5〜25重量%になるように消化水に溶解分散させ
る。この消化水を用いて生石灰を消化反応させることに
より、比表面積の大きな消石灰が得られる。この方法で
消化を行う場合は、従来の消石灰製造設備でよく、加熱
装置やアルコール回収塔などの特殊設備は必要としな
い。
First, divalent and trivalent water-soluble alcohols such as glycols and glycerins, and water-soluble amines such as primary amines, secondary amines and tertiary amines Or one or more additives selected from water-soluble sugars such as sucrose, glucose, fructose, etc., in an amount of 0.01 to 50% by weight, preferably 0.5 to 25% by weight with respect to quicklime. % And dissolve and disperse in digestion water. Slaked lime having a large specific surface area can be obtained by causing quicklime to undergo a digestion reaction using this digestion water. When digestion is performed by this method, conventional slaked lime production equipment may be used, and special equipment such as a heating device and an alcohol recovery tower is not required.

【0012】この添加剤のうち液体状のものは、消化液
に分散溶解するばかりでなく、消化前に粉末生石灰に添
加混合及び/またはコーティングしておいて、消化水を
添加し消化反応を行ってもよい。
[0012] Among these additives, those in liquid form are not only dispersed and dissolved in digestive juices, but also added and mixed and / or coated with powdered lime before digestion, and digestion reaction is performed by adding digestive water. You may.

【0013】粉末生石灰に添加剤を添加混合及び/また
はコーティングするにあたっては、粉砕された生石灰に
添加剤を加えて、ミキサー等で混合攪拌してもよいが、
生石灰を粉砕するときに、粉砕機の生石灰供給口で添加
剤を生石灰に滴下して粉砕すれば特殊装置は必要としな
い。またこの方法では、生石灰に対する添加剤の量が一
定となり、比表面積の大きい消石灰が安定して得られ
る。
In adding and mixing and / or coating the additive to the powdered lime, the additive may be added to the pulverized lime and mixed and stirred by a mixer or the like.
When crushing quicklime, a special device is not required if the additive is dropped on the quicklime at the quicklime supply port of the crusher and crushed. Further, in this method, the amount of the additive to quicklime is constant, and slaked lime having a large specific surface area can be obtained stably.

【0014】グリコール類、グリセリン類等の二価およ
び三価で水に可溶なアルコール類、第一級アミン類、第
二級アミン類および第三級アミン類で水に可溶なアミン
類、またはショ糖、ブドウ糖、果糖等の水に可溶な糖類
から選択された1種類または2種類以上を、生石灰に対
して0.02〜50重量%好ましくは0.5〜25重量
%の範囲で添加した場合比表面積増加の効果がみられ
る。この添加率は、従来の薬品の添加率に比べて、少量
の添加割合でも比表面積増大の効果が発現することが特
徴である。
Water-soluble divalent and trivalent alcohols such as glycols and glycerins, amines which are water-soluble in primary amines, secondary amines and tertiary amines; Alternatively, one or more selected from water-soluble saccharides such as sucrose, glucose, fructose, in an amount of 0.02 to 50% by weight, preferably 0.5 to 25% by weight based on quicklime. When added, the effect of increasing the specific surface area is observed. This addition rate is characterized in that the effect of increasing the specific surface area is exhibited even with a small addition rate as compared with the conventional chemical addition rate.

【0015】[0015]

【発明の実施の形態】本発明は、次のようにして実施さ
れる。〔特許請求の範囲〕の請求項1および請求項3に
おいては、まずグリコール類、グリセリン類等の二価お
よび三価で水に可溶なアルコール類、第一級アミン類、
第二級アミン類および第三級アミン類で水に可溶なアミ
ン類、またはショ糖、ブドウ糖、果糖等の水に可溶な糖
類から選択された1種類または2種類以上を生石灰に対
して0.02〜50重量%好ましくは0.5〜25重量
%になるように消化水に溶解分散させる。尚、生石灰に
たいする消化水の割合はあらかじめ調査しておく。アル
コール類等を溶解分散した消化水を消化機において生石
灰に攪拌混合しながら添加し、消化反応を行わせ消石灰
を生成させる。生成された消石灰は、従来の工程の熟成
機を経て分級機に供給され粗粉を除去されて製品とな
る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention is implemented as follows. In Claims 1 and 3 of the claims, dihydric and trivalent water-soluble alcohols such as glycols and glycerins, primary amines,
Water-soluble amines such as secondary amines and tertiary amines, or one or more selected from water-soluble sugars such as sucrose, glucose, fructose, etc. It is dissolved and dispersed in digested water so as to be 0.02 to 50% by weight, preferably 0.5 to 25% by weight. The ratio of digested water to quicklime should be investigated in advance. Digestion water in which alcohols and the like are dissolved and dispersed is added to quicklime with stirring in a digester, and a digestion reaction is performed to produce slaked lime. The generated slaked lime is supplied to a classifier through an aging machine in a conventional process, and coarse powder is removed to be a product.

【0016】しかし、この方法では連続製造している間
には、生石灰の焼成の度合いにより、消化水の添加量が
変わる場合があり得る。その場合は生石灰に対する添加
剤の割合が変化し、製品となる消石灰の比表面積または
その歩留りが変動する可能性がのこされる。そのような
ときは、〔特許請求の範囲〕の請求項1および請求項2
に示す方法によるとよい。
However, in this method, during continuous production, the amount of digested water added may vary depending on the degree of calcination of quicklime. In that case, the ratio of the additive to quick lime changes, and the specific surface area of slaked lime to be a product or the yield thereof may fluctuate. In such a case, claim 1 and claim 2 of [claims]
It is good to use the method shown in FIG.

【0017】 〔特許請求の範囲〕の請求項1および請求項2において
は添加剤をあらかじめ粉末生石灰に添加混合及び/また
はコーティングしておくことにより、生石灰に対する添
加剤の割合の安定化を図ったものである。この方法にお
いては、まずグリコール類、グリセリン類等の二価およ
び三価で水に可溶なアルコール類、第一級アミン類、第
二級アミン類および第三級アミン類で水に可溶なアミン
類から選択された1種類または2種類以上を、生石灰に
対し0.02〜50重量%好ましくは0.5〜25重量
%を粉末生石灰に添加混合及び/またはコーティングを
行う。添加剤を、添加混合及び/またはコーティングさ
れた粉末生石灰は、従来の設備で消化機において攪拌混
合しながら、消化水を添加し消化反応を行わせて、消石
灰を生成させる。生成された消石灰は、従来工程の熟成
機を経て分級機に供給され、粗粉を除去されて製品とな
る。
In claims 1 and 2 of the claims, the additive is added to the powdered lime in advance and mixed and / or coated to stabilize the ratio of the additive to quick lime. Things. In this method, first, water-soluble divalent and trivalent alcohols such as glycols and glycerins, primary amines, secondary amines and tertiary amines are used. One or more selected from amines are added to powdered lime in an amount of 0.02 to 50% by weight, preferably 0.5 to 25% by weight, based on quicklime, and mixed and / or coated. Powdered lime to which additives are mixed and / or coated is added to digestive water and digestion reaction is performed while stirring and mixing in a digester with conventional equipment to produce slaked lime. The generated slaked lime is supplied to a classifier through an aging machine in a conventional process, and coarse powder is removed to be a product.

【0018】この方法においては、長時間連続操業を行
い生石灰の状態が変動して、消化水量を調節しても、生
石灰に対する添加剤の割合はあらかじめ固定されてお
り、水量の調節により変動することなく、安定した比表
面積および歩留りが得られる。
In this method, even if the state of quick lime fluctuates due to continuous operation for a long time and the amount of digested water is adjusted, the ratio of the additive to quick lime is fixed in advance and fluctuates by adjusting the amount of water. And a stable specific surface area and yield can be obtained.

【0019】[0019]

【実施例】以下に本発明について実施例を挙げて更に詳
しく説明するが、本発明は、この例によって限定される
ものではない。
EXAMPLES The present invention will be described in more detail with reference to the following examples, but the present invention is not limited to these examples.

【0020】実施例1 粉末生石灰に対して5重量%のジエチレングリコールを
添加し、よく混合する。ジエチレングリコールを加えた
粉末生石灰105部に対して、58重量%の消化水を攪
拌しながら加えて消化、熟成を行った。
Example 1 5% by weight of diethylene glycol is added to powdered lime and mixed well. To 105 parts of powdered lime to which diethylene glycol was added, 58% by weight of digestion water was added with stirring to perform digestion and ripening.

【0021】得られた消石灰を、空気透過法によりブレ
ーン比表面積、窒素吸着法によりBET比表面積を測定
した。消石灰サンプルと燃焼ガス中の塩化水素ガスを反
応せしめる。反応後の消石灰サンプルを水に溶解させイ
オンメーターによりCa2+の濃度を、イオンクロマトグ
ラフィーによりCl- の濃度を測定し、消石灰の塩化水
素ガスとの反応率を求めた。
The obtained slaked lime was measured for a Blaine specific surface area by an air permeation method and a BET specific surface area by a nitrogen adsorption method. The slaked lime sample reacts with the hydrogen chloride gas in the combustion gas. The slaked lime sample after the reaction was dissolved in water, and the Ca 2+ concentration was measured by an ion meter and the Cl concentration was measured by ion chromatography to determine the reaction rate of slaked lime with hydrogen chloride gas.

【0022】その結果、表1に示す通り、ブレーン比表
面積40,900平方センチメートル/グラム、BET
比表面積32.4平方メートル/グラム、塩化水素ガス
との反応率28%であった。
As a result, as shown in Table 1, the specific surface area of the brane was 40,900 square centimeters / gram, and the BET
The specific surface area was 32.4 square meters / gram, and the conversion with hydrogen chloride gas was 28%.

【0023】実施例2 生石灰に対して58重量%の水に生石灰に対して5重量
%のトリエタノールアミンを溶解分散した液を消化液と
して、粉末生石灰100部に攪拌しながら添加し消化、
熟成を行った。そのブレーン比表面積、BET比表面
積、塩化水素ガスとの反応率を求めた。その結果、表1
に示す通り、ブレーン比表面積46,100平方センチ
メートル/グラム、BET比表面積39.9平方メート
ル/グラム塩化水素ガスとの反応率23%であった。
Example 2 A solution prepared by dissolving and dispersing 5% by weight of triethanolamine with respect to quick lime in water of 58% by weight with respect to quick lime was added to 100 parts of powdered quick lime with stirring to digest it.
Aging was performed. The Blaine specific surface area, BET specific surface area, and the reaction rate with hydrogen chloride gas were determined. As a result, Table 1
As shown in the figure, the specific surface area was 46,100 square centimeters / gram, and the BET specific surface area was 39.9 square meters / gram. The conversion with hydrogen chloride gas was 23%.

【0024】実施例3 生石灰に対して50重量%の水に生石灰に対して4重量
%のショ糖を溶解分散した液を消化液として、生石灰1
00部に攪拌しながら添加し消化、熟成を行った後、分
級して細粉消石灰を得た。そのブレーン比表面積、BE
T比表面積、塩化水素ガスとの反応率を求めた。その結
果、表1に示すとおり、ブレーン比表面積56,900
平方センチメートル/グラム、BET比表面積22.9
平方メートル/グラム、塩化水素ガスとの反応率36%
であった。
Example 3 A solution prepared by dissolving and dispersing 4% by weight of sucrose in water of 50% by weight of quicklime in a water of 50% by weight of quicklime was used as a digestive solution to prepare quicklime 1
The mixture was added to 00 parts with stirring, digested and aged, and then classified to obtain fine powder slaked lime. Its brain specific surface area, BE
The T specific surface area and the reaction rate with hydrogen chloride gas were determined. As a result, as shown in Table 1, the Blaine specific surface area was 56,900.
Square centimeter / gram, BET specific surface area 22.9
Square meter / gram, reaction rate with hydrogen chloride gas 36%
Met.

【0025】比較例1 生石灰100部に対して、52重量%の水を攪拌しなが
ら添加し消化、熟成させるた後分級し細粉消石灰を得
た。そのブレーン比表面積、BET比表面積、塩化水素
ガスとの反応率を求めた。その結果、表1に示すとお
り、ブレーン比表面積22,300平方センチメートル
/グラム、BET比表面積12.1平方メートル/グラ
ム、塩化水素ガスとの反応率6%であった。
Comparative Example 1 To 100 parts of quicklime, 52% by weight of water was added with stirring, digested and aged, and classified to obtain fine powdered slaked lime. The Blaine specific surface area, BET specific surface area, and the reaction rate with hydrogen chloride gas were determined. As a result, as shown in Table 1, the Blaine specific surface area was 22,300 square centimeters / gram, the BET specific surface area was 12.1 square meters / gram, and the reaction rate with hydrogen chloride gas was 6%.

【0026】[0026]

【表1】 [Table 1]

【0027】[0027]

【発明の効果】以上詳述した通り、本発明の消石灰の製
造方法によれば、従来法に比較して、比表面積が大き
く、塩化水素ガスとの反応性が大きい消石灰を製造する
ことができる。本発明で得られる消石灰によれば、塵芥
焼却炉の燃焼ガスなどの処理にあたり、塩化水素ガス等
の除去を効率的に行うことができ、消石灰の使用量が従
来の消石灰より、少なくて済ませることが可能になる。
その結果、発生するダストの量を低減することが可能に
なり、廃棄物の処理場の寿命を延命することが可能とな
る。
As described in detail above, according to the method for producing slaked lime of the present invention, slaked lime having a large specific surface area and a high reactivity with hydrogen chloride gas can be produced as compared with the conventional method. . According to the slaked lime obtained in the present invention, it is possible to efficiently remove hydrogen chloride gas and the like in the treatment of combustion gas and the like in a garbage incinerator, and to use less slaked lime than conventional slaked lime. Becomes possible.
As a result, the amount of generated dust can be reduced, and the life of the waste treatment plant can be extended.

【0028】また、本発明方法は、加熱装置やアルコー
ル回収塔等の特殊設備は必要とせず、添加剤の供給のた
めの設備を追加するだけで従来の消化設備で実施するこ
とが可能で、工業的に容易かつ効率的に行うととができ
る。
Further, the method of the present invention does not require special equipment such as a heating device and an alcohol recovery tower, and can be carried out with conventional digestion equipment only by adding equipment for supplying additives. It can be carried out industrially easily and efficiently.

【0029】請求項1、2の消石灰の製造方法によれ
ば、より一層安定かつ効率的に高比表面積消石灰を得る
ことが可能である。
According to the method for producing slaked lime of the first and second aspects, slaked lime having a high specific surface area can be obtained more stably and efficiently.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 天野 克彦 滋賀県坂田郡山東町長岡1780番地 近江鉱 業株式会 社 (72)発明者 加田 松藏 滋賀県坂田郡山東町長岡1780番地 近江鉱 業株式会 社 (72)発明者 宮山 孝一 滋賀県坂田郡山東町長岡1780番地 近江鉱 業株式会 社 (72)発明者 巨椋 徳文 滋賀県坂田郡山東町長岡1780番地 近江鉱 業株式会 社 (72)発明者 星山 勝彦 滋賀県坂田郡山東町長岡1780番地 近江鉱 業株式会 社 ──────────────────────────────────────────────────の Continuing on the front page (72) Katsuhiko Amano, Inventor 1780 Nagaoka, Yamato-cho, Sakata-gun, Shiga Prefecture Omi Mining Co., Ltd. (72) Matsuzo Matsuda 1780, Nagaoka, Yamato-cho, Sakata-gun, Shiga Prefecture Omi Mining Co., Ltd. (72) Inventor Koichi Miyayama 1780 Nagaoka, Yamato-cho, Sakata-gun, Shiga Prefecture Omi Mining Co., Ltd. (72) Inventor Tokufumi Ogura 1780, Nagaoka, Yamato-cho, Sakata-gun, Shiga Prefecture Omi Mining Co., Ltd. (72) Inventor Katsuhiko Hoshiyama 1780 Nagaoka, Yamato-cho, Sakata-gun, Japan Omi Mining Co., Ltd.

Claims (7)

【申請人整理番号】 OA107 【特許請求の範囲】[Applicant Reference Number] OA107 [Claims] 【請求項1】 消石灰及び、アルコール類、アミン類ま
たは糖類の内から選択された1種類または2種類以上の
添加剤からなることを特徴とする高反応性消石灰。
1. Highly reactive slaked lime comprising slaked lime and one or more additives selected from alcohols, amines and saccharides.
【請求項2】 粉末生石灰に、アルコール類、アミン類
の1種類または2種類以上を生石灰に対して0.02〜
50重量%好ましくは0.5〜25重量%添加混合及び
/またはコーティングした状態で、消化水を加えて消化
反応させることを特徴とする請求項1記載の高反応性消
石灰の製造方法。
2. Powdered lime is added with one or two or more of alcohols and amines in an amount of 0.02 to lime.
The method for producing highly reactive slaked lime according to claim 1, wherein digestion reaction is performed by adding digestion water in a mixed and / or coated state of 50% by weight, preferably 0.5 to 25% by weight.
【請求項3】 生石灰に、アルコール類、アミン類、糖
類の1種類または2種類以上を生石灰に対して0.02
〜50重量%好ましくは0.5〜25重量%を溶解した
水を消化水として添加し消化反応させることを特徴とす
る請求項1記載の高反応性消石灰の製造方法。
3. The quicklime contains one or more of alcohols, amines and sugars in an amount of 0.02 to quicklime.
The method for producing highly reactive slaked lime according to claim 1, characterized in that water having dissolved therein 50 to 50% by weight, preferably 0.5 to 25% by weight, is added as digestion water to cause a digestion reaction.
【請求項4】 生石灰を粉砕するときに、アルコール
類、アミン類の1種類または2種類以上を添加すること
により生石灰をコーティングすることを特徴とする請求
項1および請求項2記載の高反応性消石灰の製造方法。
4. The highly reactive lime according to claim 1, wherein when crushing quick lime, quick lime is coated by adding one or more of alcohols and amines. A method for producing slaked lime.
【請求項5】 アルコール類がグリコール類、グリセリ
ン類等の二価および三価で水に可溶なアルコールである
ことを特徴とする請求項1〜請求項4記載の高反応性消
石灰の製造方法。
5. The method for producing highly reactive slaked lime according to claim 1, wherein the alcohol is a bivalent and trivalent water-soluble alcohol such as glycols and glycerins. .
【請求項6】 アミン類が第一級アミン類、第二級アミ
ン類及び第三級アミン類で水に可溶なアミンであること
を特徴とする請求項1〜請求項4記載の高反応性消石灰
の製造方法。
6. The high reaction according to claim 1, wherein the amine is a primary amine, a secondary amine or a tertiary amine and is soluble in water. Method for producing hydrated slaked lime.
【請求項7】 糖類がショ糖、ブドウ糖、果糖等の水に
可溶な糖類であることを特徴とする請求項1および請求
項3記載の高反応性消石灰の製造方法。
7. The method for producing highly reactive slaked lime according to claim 1, wherein the saccharide is a water-soluble saccharide such as sucrose, glucose and fructose.
JP27707696A 1996-09-27 1996-09-27 High reactivity slaked lime and its production Pending JPH10101331A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27707696A JPH10101331A (en) 1996-09-27 1996-09-27 High reactivity slaked lime and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27707696A JPH10101331A (en) 1996-09-27 1996-09-27 High reactivity slaked lime and its production

Publications (1)

Publication Number Publication Date
JPH10101331A true JPH10101331A (en) 1998-04-21

Family

ID=17578449

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27707696A Pending JPH10101331A (en) 1996-09-27 1996-09-27 High reactivity slaked lime and its production

Country Status (1)

Country Link
JP (1) JPH10101331A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003002643A (en) * 2001-06-22 2003-01-08 Tosoh Corp Slaked lime having high specific surface area, producing method therefor, and use thereof
JP2003026420A (en) * 2001-07-17 2003-01-29 Tosoh Corp High-specific-surface-area slaked lime and method of manufacturing the same and application of the same
JP2003081631A (en) * 2001-09-10 2003-03-19 Tosoh Corp High specific surface area slaked lime, production method therefor, and its use
JP2012130323A (en) * 2010-12-24 2012-07-12 Karushin:Kk Solution of highly dissolvable calcium hydroxide, and powder thereof
US11365150B1 (en) * 2018-07-18 2022-06-21 Mississippi Lime Company Lime hydrate with improved reactivity via additives

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003002643A (en) * 2001-06-22 2003-01-08 Tosoh Corp Slaked lime having high specific surface area, producing method therefor, and use thereof
JP2003026420A (en) * 2001-07-17 2003-01-29 Tosoh Corp High-specific-surface-area slaked lime and method of manufacturing the same and application of the same
JP2003081631A (en) * 2001-09-10 2003-03-19 Tosoh Corp High specific surface area slaked lime, production method therefor, and its use
JP2012130323A (en) * 2010-12-24 2012-07-12 Karushin:Kk Solution of highly dissolvable calcium hydroxide, and powder thereof
US11365150B1 (en) * 2018-07-18 2022-06-21 Mississippi Lime Company Lime hydrate with improved reactivity via additives

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