JPH0717711A - Highly active calcium oxide and powdering agent - Google Patents
Highly active calcium oxide and powdering agentInfo
- Publication number
- JPH0717711A JPH0717711A JP6021439A JP2143994A JPH0717711A JP H0717711 A JPH0717711 A JP H0717711A JP 6021439 A JP6021439 A JP 6021439A JP 2143994 A JP2143994 A JP 2143994A JP H0717711 A JPH0717711 A JP H0717711A
- Authority
- JP
- Japan
- Prior art keywords
- calcium oxide
- highly active
- active calcium
- water
- firing
- 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
Landscapes
- Fodder In General (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
(57)【要約】
【目的】 この発明は、含水物の溶解成分を損なうこと
なく、かつ当該含水物の溶解成分を性状変性させること
なく微粉末化させ得る高活性を有する高活性酸化カルシ
ウムを得ることを目的としたものである。
【構成】 卵殻を900℃〜1500℃で焼成して得た
高活性酸化カルシウム。卵殻を900℃〜1500℃で
焼成して得た高活性酸化カルシウムからなる粉末化剤。(57) [Abstract] [Object] The present invention provides a highly active calcium oxide having a high activity that can be made into fine powder without impairing the dissolved component of a hydrous substance and without modifying the dissolved component of the hydrous substance. The purpose is to obtain. [Structure] Highly active calcium oxide obtained by firing egg shells at 900 ° C to 1500 ° C. A powdering agent comprising highly active calcium oxide obtained by firing egg shells at 900 ° C to 1500 ° C.
Description
【0001】[0001]
【産業上の利用分野】この発明は、卵殻を高温処理して
得た高活性酸化カルシウムに関する。また、この発明
は、卵殻を高温処理して得た高活性酸化カルシウムから
なる粉末化剤に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to highly active calcium oxide obtained by treating egg shells at a high temperature. The present invention also relates to a powdering agent composed of highly active calcium oxide obtained by treating egg shells at a high temperature.
【0002】[0002]
【従来の技術】従来、貝殻を高温処理して得られた酸化
カルシウムは知られていた。これは、工業生産におい
て、貝殻を900℃〜1000℃で処理して生産するの
が通例であった。2. Description of the Related Art Calcium oxide obtained by treating shells at a high temperature has been known. In the industrial production, it is customary to treat shells at 900 ° C to 1000 ° C for production.
【0003】[0003]
【発明により解決すべき課題】前記従来の貝殻を高温処
理して得られた酸化カルシウムでは、活性が改善される
ことが知られていたが、どのような活性の改善があるの
かは、従来は不明であった。It has been known that calcium oxide obtained by subjecting the conventional shells to high temperature treatment has improved activity. What kind of activity improvement is conventionally known? It was unknown.
【0004】また、生石灰(酸化カルシウム)に水を付
与すると消石灰(水酸化カルシウム)になることが知ら
れているが、付与する水の量が多いと泥状になり、また
少ないと不均一な粉末状態となり、全体を均一な粉末と
することは困難であった。It is also known that when water is added to quicklime (calcium oxide), it becomes slaked lime (calcium hydroxide). If the amount of water added is large, it becomes muddy, and if it is small, it is uneven. It became a powder state and it was difficult to make the whole into a uniform powder.
【0005】[0005]
【課題を解決する為の手段】本願の第一の発明は、卵殻
を900℃〜1500℃で焼成して得た高活性酸化カル
シウムである。また、第二の発明は、卵殻を1200℃
〜1300℃で焼成して得た高活性酸化カルシウムであ
る。本願の第三の発明は、卵殻を900℃〜1500℃
で焼成して得た高活性酸化カルシウムからなる粉末化剤
である。また、第四の発明は、卵殻を1200℃〜13
00℃で焼成して得た高活性酸化カルシウムからなる粉
末化剤である。The first invention of the present application is a highly active calcium oxide obtained by baking egg shells at 900 ° C to 1500 ° C. The second invention is that the eggshell is 1200 ° C.
It is a highly active calcium oxide obtained by firing at ~ 1300 ° C. 3rd invention of this application WHEREIN: 900 degreeC-1500 degreeC of eggshell
It is a powdering agent composed of highly active calcium oxide obtained by firing at. Moreover, 4th invention WHEREIN: 1200 degreeC-13 degree
It is a powdering agent composed of highly active calcium oxide obtained by firing at 00 ° C.
【0006】本願のこれらの発明によって得られた高活
性酸化カルシウムは、従来知られていた酸化カルシウム
と異なり、含水物と重量比でほぼ等量ずつ混合すると激
しく反応し、当該含水物の溶解成分を損なうことなく、
かつ当該含水物の溶解成分を性状変性させることなく微
粉末化させることができた。The highly active calcium oxide obtained by these inventions of the present application, unlike conventionally known calcium oxide, reacts violently when mixed with a hydrous substance in substantially equal weight ratios, and a dissolved component of the hydrous substance. Without compromising
In addition, the dissolved component of the water-containing material could be made into fine powder without property modification.
【0007】また、この高活性酸化カルシウムからなる
本願発明の粉末化剤も同じく、含水物と重量比でほぼ等
量ずつ混合すると激しく反応し、当該含水物の溶解成分
を損なうことなく、かつ当該含水物の溶解成分を性状変
性させることなく微粉末化させることができる。Also, the powdering agent of the present invention composed of this highly active calcium oxide also reacts violently when mixed with the hydrous material in approximately equal weight ratios, without impairing the dissolved components of the hydrous material, and The dissolved component of the water-containing material can be made into fine powder without changing the properties.
【0008】前記において、含水物とは、水溶液や水を
含むものであればよく、水を含んでいない場合、例えば
油脂類のような場合には、水を懸濁すればよい。以下、
本明細書において含水物というときは、水溶液や水を含
むものの他、このように水を含んでいなくても水に懸濁
すればよいものをも含むものとする。In the above description, the water-containing material may be any solution containing water or water, and when it does not contain water, such as fats and oils, water may be suspended. Less than,
In the present specification, the term "water-containing material" includes not only water solutions and water-containing materials but also those that do not contain water and can be suspended in water.
【0009】前記において、焼成温度が900℃未満の
場合には、活性不足のために、得られたカルシウムを含
水物と混合した場合に、当該含水物は泥状となり、微粉
末化させることはできない。900℃以上で、焼成処理
した場合には、得られた高活性酸化カルシウムは前述し
た活性を有し、含水物と重量比でほぼ等量ずつ混合する
と激しく反応し、当該含水物の溶解成分を損なうことな
く、また溶解成分を性状変性させることなく微粉末化さ
せることができる。ただし、1000℃以下で焼成処理
した場合には、得られた高活性酸化カルシウムを含水物
と混合した場合の反応速度はゆっくりであり、1000
℃以上で焼成処理した場合には、反応速度はこれ以下の
焼成温度の場合より次第に速くなる。一方、1500℃
で焼成処理した場合の反応速度は、1300℃で焼成処
理した場合とほとんど変わらなくなる。そこで、本願発
明の高活性酸化カルシウムを得るために卵殻を焼成する
温度は900℃〜1500℃であることが好ましい。も
っとも、1500℃で焼成処理した場合の反応速度が、
1300℃で焼成処理した場合とほとんど変わらなくな
ることから、効率のよさ及び費用の観点から、最も好ま
しい焼成温度の上限を1300℃に設定することができ
る。一方、900℃から焼成温度が高くなるにつれて、
得られる高活性酸化カルシウムの反応速度は次第に速く
なるわけであるが、発明者の実験によれば、得られた高
活性酸化カルシウムを含水物と混合した場合の反応速度
の速さの観点から見ると、焼成処理の温度の最も好まし
い範囲の下限は1200℃となった。[0009] In the above, when the firing temperature is lower than 900 ° C, due to lack of activity, when the obtained calcium is mixed with a water-containing material, the water-containing material becomes a mud and is not finely pulverized. Can not. When calcined at 900 ° C. or higher, the obtained highly active calcium oxide has the above-mentioned activity, and when mixed with a hydrous substance in approximately equal amounts by weight, it reacts violently to dissolve dissolved components of the hydrous substance. It is possible to make fine powder without damaging the dissolved component without modifying its properties. However, when the calcination treatment is performed at 1000 ° C. or lower, the reaction rate when the obtained highly active calcium oxide is mixed with a water-containing substance is slow,
When the baking treatment is performed at a temperature of ℃ or higher, the reaction rate becomes gradually higher than that at a baking temperature lower than this. Meanwhile, 1500 ° C
The reaction rate in the case of the baking treatment at 1 is almost the same as that in the case of the baking treatment at 1300 ° C. Therefore, the temperature for firing the egg shell to obtain the highly active calcium oxide of the present invention is preferably 900 ° C to 1500 ° C. However, the reaction rate when firing at 1500 ° C is
Since there is almost no difference from the case of firing at 1300 ° C, the most preferable upper limit of the firing temperature can be set to 1300 ° C from the viewpoint of efficiency and cost. On the other hand, as the firing temperature increases from 900 ° C,
The reaction rate of the obtained highly active calcium oxide gradually increases, but according to the experiments of the inventor, it is seen from the viewpoint of the reaction rate when the obtained highly active calcium oxide is mixed with a hydrate. Then, the lower limit of the most preferable range of the firing temperature was 1200 ° C.
【0010】また、発明者の実験によれば、1200℃
〜1300℃の焼成温度で得られた高活性酸化カルシウ
ムは、他の温度範囲で焼成して得られた高活性酸化カル
シウムと比較した場合、含水物を微粉末化させるという
活性が安定している。すなわち、本願発明で得られた高
活性酸化カルシウムの中には、生成後時間が経過するに
つれて、含水物を微粉末化させるという活性が不安定に
なるものがある。例えば、含水物を微粉末化させること
は依然としてできるのだが、生成後あまり時間が経過し
ないうちに使用された場合に粉末化に要する時間より
も、生成後ある程度時間が経過してから使用された際に
粉末化に要する時間のほうが長くなるといったものがあ
る。しかし、1200℃〜1300℃の焼成温度で得ら
れた高活性酸化カルシウムは、生成後時間が経過して
も、含水物を微粉末化させるという活性が安定してお
り、他の温度範囲で焼成して得られた本願発明の高活性
酸化カルシウムと比較した場合、この安定性が最も優れ
ていた。Further, according to an experiment conducted by the inventor, 1200 ° C.
The highly active calcium oxide obtained at a calcination temperature of ˜1300 ° C. has a stable activity of making the hydrated substance into a fine powder when compared with the highly active calcium oxide obtained by calcination at other temperature ranges. . That is, among the highly active calcium oxides obtained in the present invention, there is one in which the activity of making the hydrated substance into a fine powder becomes unstable as time passes after generation. For example, although it is still possible to pulverize a water-containing material into fine powder, it was used after a certain amount of time had elapsed after the formation, rather than the time required for pulverization if it was used within a short time after the formation. In some cases, the time required for pulverization becomes longer. However, the highly active calcium oxide obtained at a calcination temperature of 1200 ° C to 1300 ° C has a stable activity of pulverizing the hydrous material even after a lapse of time after generation, and is calcined at other temperature ranges. When compared with the highly active calcium oxide of the present invention obtained in this way, this stability was the most excellent.
【0011】前記において、本願発明によって得られた
高活性酸化カルシウムあるいはこの高活性酸化カルシウ
ムからなる粉末化剤と含水物との混合割合を、重量比で
ほぼ等量ずつとした理由は、かかる割合が粉末化反応の
促進に最適であり、またかかる割合によれば粉末化反応
によって得られた粉末中に、含水物などの有効成分が最
もよく含有され得るからである。本願発明者の実験によ
れば、本願発明の高活性酸化カルシウムあるいはこの高
活性酸化カルシウムからなる粉末化剤1重量部に対し
て、含水物0.3〜3.3重量部程度の範囲の混合割合
で粉末化反応が生じた。これは、含水物の種類によって
も相違し、例えば、血液の場合には、本願発明の高活性
酸化カルシウムあるいはこの高活性酸化カルシウムから
なる粉末化剤1重量部に対して血液0.6〜3.3重量
部程度の範囲の混合割合で粉末化反応が生じた。また、
液状油脂類の場合には、本願発明の高活性酸化カルシウ
ムあるいはこの高活性酸化カルシウムからなる粉末化剤
1重量部に対して液状油脂類0.3〜1.7重量部程度
の範囲の混合割合で粉末化反応が生じた。In the above, the reason why the mixing ratio of the highly active calcium oxide obtained by the present invention or the powdering agent composed of this highly active calcium oxide and the hydrate is approximately equal in weight ratio is the ratio. Is most suitable for accelerating the pulverization reaction, and at such a ratio, the powder obtained by the pulverization reaction can contain the active ingredient such as a hydrous substance most. According to the experiments conducted by the inventor of the present application, the highly active calcium oxide of the present invention or 1 part by weight of the powdering agent composed of this highly active calcium oxide is mixed in the range of about 0.3 to 3.3 parts by weight of the hydrate. A powdering reaction occurred in proportion. This differs depending on the kind of the hydrated substance. For example, in the case of blood, 0.6 to 3 parts of blood are added to 1 part by weight of the highly active calcium oxide of the present invention or a powdering agent composed of this highly active calcium oxide. The powdering reaction occurred at a mixing ratio of about 0.3 part by weight. Also,
In the case of liquid oils and fats, the mixing ratio of the liquid oils and fats in the range of 0.3 to 1.7 parts by weight to 1 part by weight of the highly active calcium oxide of the present invention or the powdering agent composed of this highly active calcium oxide. A powdering reaction occurred at.
【0012】[0012]
【作用】このように、本願発明で得られる高活性酸化カ
ルシウム及びこの高活性酸化カルシウムからなる粉末化
剤は、水分が加えられることによって、急速に反応し、
微粉末化する。この微粉末化は、水分のみでもよいが、
酸性水(例えば木酢液など)を加えるほうが、より急激
な反応が見られる。この高活性酸化カルシウム及び当該
高活性酸化カルシウムからなる粉末化剤は、特に血液な
どの粘性液体、あるいは、動物油脂、植物油脂、鉱物油
脂などの液状油脂類の粉末化には顕著に有効である。ま
た、混合された含水物の溶解成分を損なうことなく、か
つ当該含水物の溶解成分を性状変性させることなく微粉
末化させることができる。したがって、微粉末化するこ
とが困難な液状物質を有効成分を保有させたまま粉末化
させるについては、多大の効果がある。この微粉末化反
応は、反応熱を生じるのみであって、乾燥その他の操作
を加える必要はない。As described above, the highly active calcium oxide obtained in the present invention and the powdering agent composed of this highly active calcium oxide react rapidly when water is added,
Micronize. This pulverization may be water only,
A more rapid reaction can be seen by adding acidic water (such as wood vinegar). The highly active calcium oxide and the powdering agent composed of the highly active calcium oxide are remarkably effective for powdering viscous liquids such as blood, or liquid oils and fats such as animal oils, vegetable oils and mineral oils. . In addition, it is possible to make fine powder without damaging the dissolved components of the mixed hydrous material and without modifying the properties of the dissolved components of the hydrous material. Therefore, there is a great effect in pulverizing a liquid substance that is difficult to be pulverized while retaining the active ingredient. This pulverization reaction only generates heat of reaction and does not require drying or other operations.
【0013】[0013]
【実施例1】水洗した白色卵殻を自然乾燥あるいは人工
乾燥し、この卵殻片40kgを電気炉で、通風雰囲気化
(80cm3 / min)において、900℃で5時間焼成
し、その後、自然冷却させた。こうして得た焼成処理後
の白色卵殻片を微粉砕し、1mm以下の粉末にして高活性
酸化カルシウム約20kgを得た。Example 1 A white egg shell washed with water was naturally or artificially dried, and 40 kg of this egg shell piece was fired in an electric furnace at 900 ° C. for 5 hours in a ventilated atmosphere (80 cm 3 / min), and then naturally cooled. It was The white egg shell pieces thus obtained after calcination were finely pulverized into powder of 1 mm or less to obtain about 20 kg of highly active calcium oxide.
【0014】前記において、焼成時間を5時間とした理
由は、電気炉内の卵殻片を均一に900℃で焼成するの
に必要なためである。すなわち、焼成時間は電気炉内の
卵殻片を一定温度で均一に焼成するために必要とされる
時間であるので、卵殻片の量、焼成温度などに応じて定
められる。In the above description, the reason for setting the firing time to 5 hours is that it is necessary to uniformly fire the eggshell pieces in the electric furnace at 900.degree. That is, the firing time is the time required to evenly fire the eggshell pieces in the electric furnace at a constant temperature, and is determined according to the amount of eggshell pieces, the firing temperature, and the like.
【0015】また、焼成後の卵殻片を1mm以下の粉末に
微粉砕した理由は、得られた高活性酸化カルシウムの粉
末化反応によってできる生成物が均一の生成物になるよ
うにするためであり、また粉末化の反応速度を早くさせ
るためである。The reason why the egg shell pieces after firing were finely pulverized to a powder of 1 mm or less was to ensure that the product formed by the powdering reaction of the obtained highly active calcium oxide was a uniform product. This is also for increasing the reaction speed of powdering.
【0016】この生成された高活性酸化カルシウムの活
性を検討すべく、高活性酸化カルシウム100gに同量
(100g、100ml)の木酢液を加入し、30秒間撹
拌し、静置した。時間の経過と共に泥状の混合物の表面
に木酢液が少し浮いてきて、静置後10分し、泥状の混
合物の表面に亀裂ができ、水分が蒸発し、微粉末のCa
結合の木酢酸粉末ができた。In order to examine the activity of the produced high-activity calcium oxide, the same amount (100 g, 100 ml) of wood vinegar solution was added to 100 g of high-activity calcium oxide, stirred for 30 seconds and allowed to stand. The wood vinegar slightly floated on the surface of the mud-like mixture with the passage of time, and after 10 minutes of standing, cracks were formed on the surface of the mud-like mixture, water vaporized, and fine powder of Ca was formed.
A combined wood acetic acid powder was created.
【0017】こうして得られた微粉末中の木酢液の成分
を調べたところ、添加された高活性酸化カルシウムと結
合した木酢液の成分と認められた。When the components of the wood vinegar solution in the fine powder thus obtained were examined, it was recognized as the components of the wood vinegar solution combined with the added highly active calcium oxide.
【0018】[0018]
【実施例2】水洗した白色卵殻を自然乾燥あるいは人工
乾燥し、この卵殻片40kgを電気炉で通風雰囲気化(8
0cm3 / min)において1000℃で5時間焼成し、そ
の後、自然冷却させた。こうして得た焼成処理後の白色
卵殻片を微粉砕し、1mm以下の粉末にして高活性酸化カ
ルシウム約20kgを得た。Example 2 A white egg shell washed with water was naturally or artificially dried, and 40 kg of this egg shell piece was placed in a ventilated atmosphere in an electric furnace (8
It was calcined at 0 ° C. 3 / min) at 1000 ° C. for 5 hours and then naturally cooled. The white egg shell pieces thus obtained after calcination were finely pulverized into powder of 1 mm or less to obtain about 20 kg of highly active calcium oxide.
【0019】前記において、焼成時間を5時間とした理
由は、電気炉内の卵殻片を均一に1000℃で焼成する
のに必要なためである。In the above, the reason for setting the firing time to 5 hours is that it is necessary to uniformly fire the eggshell pieces in the electric furnace at 1000.degree.
【0020】また、焼成後の卵殻片を1mm以下の粉末に
微粉砕した理由は、得られた高活性酸化カルシウムの粉
末化反応によってできる生成物が均一の生成物になるよ
うにするためであり、また粉末化の反応速度を早くさせ
るためである。The reason why the egg shell pieces after firing were finely pulverized to a powder of 1 mm or less was to ensure that the product obtained by the pulverization reaction of the obtained highly active calcium oxide was a uniform product. This is also for increasing the reaction speed of powdering.
【0021】この生成された高活性酸化カルシウムの活
性を検討すべく、高活性酸化カルシウム100gに同量
(100g、100ml)の木酢液を加入し、30秒間撹
拌し、静置した。時間の経過と共に泥状の混合物の表面
に木酢液が少し浮いてきて、静置後約7分し、泥状の混
合物の表面に亀裂ができ、水分が蒸発し、瞬間的に均一
な微粉末のCa結合の木酢酸粉末ができた。In order to examine the activity of the produced high-activity calcium oxide, the same amount (100 g, 100 ml) of wood vinegar solution was added to 100 g of high-activity calcium oxide, stirred for 30 seconds and allowed to stand. The wood vinegar solution floated a little on the surface of the mud-like mixture with the passage of time, and after standing for about 7 minutes, cracks were formed on the surface of the mud-like mixture, the water vaporized, and a momentarily uniform fine powder. A Ca-bonded wood acetic acid powder was prepared.
【0022】こうして得られた微粉末中の木酢液の成分
を調べたところ、添加された高活性酸化カルシウムと結
合した木酢液の成分と認められた。When the components of the wood vinegar solution in the fine powder thus obtained were examined, it was recognized as the components of the wood vinegar solution combined with the added highly active calcium oxide.
【0023】[0023]
【実施例3】水洗した白色卵殻を自然乾燥あるいは人工
乾燥し、この卵殻片40kgを電気炉で通風雰囲気化(8
0cm3 / min)において1100℃で5時間焼成し、そ
の後、自然冷却させた。こうして得た焼成処理後の白色
卵殻片を微粉砕し、1mm以下の粉末にして高活性酸化カ
ルシウム約20kgを得た。Example 3 A white egg shell washed with water was naturally or artificially dried, and 40 kg of this egg shell piece was placed in a ventilated atmosphere in an electric furnace (8
It was calcined at 1100 ° C. for 5 hours at 0 cm 3 / min) and then naturally cooled. The white egg shell pieces thus obtained after calcination were finely pulverized into powder of 1 mm or less to obtain about 20 kg of highly active calcium oxide.
【0024】前記において、焼成時間を5時間とした理
由は、電気炉内の卵殻片を均一に1100℃で焼成する
のに必要なためである。In the above, the reason for setting the baking time to 5 hours is that it is necessary for baking the eggshell pieces in the electric furnace uniformly at 1100.degree.
【0025】また、焼成後の卵殻片を1mm以下の粉末に
微粉砕した理由は、得られた高活性酸化カルシウムの粉
末化反応によってできる生成物が均一の生成物になるよ
うにするためであり、また粉末化の反応速度を早くさせ
るためである。The reason why the egg shell pieces after firing were finely pulverized to a powder of 1 mm or less was to ensure that the product obtained by the powdering reaction of the obtained highly active calcium oxide was a uniform product. This is also for increasing the reaction speed of powdering.
【0026】この生成された高活性酸化カルシウムの活
性を検討すべく、高活性酸化カルシウム100gに同量
(100g、100ml)の木酢液を加入し、30秒間撹
拌し、静置した。時間の経過と共に泥状の混合物の表面
に木酢液が少し浮いてきて、静置後約7分し、泥状の混
合物の表面に亀裂ができ、水分が蒸発し、瞬間的に均一
な微粉末のCa結合の木酢酸粉末ができた。In order to study the activity of the produced high-activity calcium oxide, the same amount (100 g, 100 ml) of wood vinegar was added to 100 g of high-activity calcium oxide, stirred for 30 seconds and allowed to stand. The wood vinegar solution floated a little on the surface of the mud-like mixture with the passage of time, and after standing for about 7 minutes, cracks were formed on the surface of the mud-like mixture, the water vaporized, and a momentarily uniform fine powder. A Ca-bonded wood acetic acid powder was prepared.
【0027】こうして得られた微粉末中の木酢液の成分
を調べたところ、添加された高活性酸化カルシウムと結
合した木酢液の成分と認められた。When the components of the wood vinegar solution in the fine powder thus obtained were examined, it was recognized as the components of the wood vinegar solution combined with the added highly active calcium oxide.
【0028】[0028]
【実施例4】水洗した白色卵殻を自然乾燥あるいは人工
乾燥し、この卵殻片40kgを電気炉で通風雰囲気化(8
0cm3 / min)において1200℃で5時間焼成し、そ
の後、自然冷却させた。こうして得た焼成処理後の白色
卵殻片を微粉砕し、1mm以下の粉末にして高活性酸化カ
ルシウム約20kgを得た。Example 4 A white egg shell washed with water was naturally or artificially dried, and 40 kg of this egg shell piece was placed in a ventilated atmosphere in an electric furnace (8
It was baked at 1200 ° C. for 5 hours at 0 cm 3 / min) and then naturally cooled. The white egg shell pieces thus obtained after calcination were finely pulverized into powder of 1 mm or less to obtain about 20 kg of highly active calcium oxide.
【0029】前記において、焼成時間を5時間とした理
由は、電気炉内の卵殻片を均一に1200℃で焼成する
のに必要なためである。In the above, the reason for setting the baking time to 5 hours is that it is necessary for baking the eggshell pieces in the electric furnace uniformly at 1200.degree.
【0030】また、焼成後の卵殻片を1mm以下の粉末に
微粉砕した理由は、得られた高活性酸化カルシウムの粉
末化反応によってできる生成物が均一の生成物になるよ
うにするためであり、また粉末化の反応速度を早くさせ
るためである。The reason why the egg shell pieces after firing were finely pulverized to a powder of 1 mm or less was to ensure that the product obtained by the powdering reaction of the obtained highly active calcium oxide was a uniform product. This is also for increasing the reaction speed of powdering.
【0031】この生成された高活性酸化カルシウムの活
性を検討すべく、高活性酸化カルシウム100gに同量
(100g、100ml)の木酢液を加入し、30秒間撹
拌し、静置した。時間の経過と共に泥状の混合物の表面
に木酢液が少し浮いてきて、静置後約6分し、泥状の混
合物の表面に亀裂ができ、水分が蒸発し、瞬間的に均一
な微粉末のCa結合の木酢酸粉末ができた。In order to examine the activity of the produced highly active calcium oxide, the same amount (100 g, 100 ml) of wood vinegar was added to 100 g of highly active calcium oxide, stirred for 30 seconds and allowed to stand. The wood vinegar solution floated a little on the surface of the mud-like mixture with the passage of time, and after standing for about 6 minutes, cracks were formed on the surface of the mud-like mixture, the water vaporized, and a momentarily uniform fine powder. A Ca-bonded wood acetic acid powder was prepared.
【0032】こうして得られた微粉末中の木酢液の成分
を調べたところ、添加された高活性酸化カルシウムと結
合した木酢液の成分と認められた。When the components of the wood vinegar solution in the fine powder thus obtained were examined, it was recognized as the components of the wood vinegar solution combined with the added highly active calcium oxide.
【0033】[0033]
【実施例5】水洗した白色卵殻を自然乾燥あるいは人工
乾燥し、この卵殻片40kgを電気炉で通風雰囲気化(8
0cm3 / min)において1300℃で4時間焼成し、そ
の後、自然冷却させた。こうして得た焼成処理後の白色
卵殻片を微粉砕し、1mm以下の粉末にして高活性酸化カ
ルシウム約20kgを得た。[Embodiment 5] White eggshells washed with water are naturally dried or artificially dried, and 40 kg of the eggshell pieces are placed in a ventilated atmosphere in an electric furnace (8
It was baked at 1300 ° C. for 4 hours at 0 cm 3 / min) and then naturally cooled. The white egg shell pieces thus obtained after calcination were finely pulverized into powder of 1 mm or less to obtain about 20 kg of highly active calcium oxide.
【0034】前記において、焼成時間を4時間とした理
由は、電気炉内の卵殻片を均一に1300℃で焼成する
のに必要なためである。In the above, the reason for setting the firing time to 4 hours is that it is necessary to uniformly fire the eggshell pieces in the electric furnace at 1300.degree.
【0035】また、焼成後の卵殻片を1mm以下の粉末に
微粉砕した理由は、得られた高活性酸化カルシウムの粉
末化反応によってできる生成物が均一の生成物になるよ
うにするためであり、また粉末化の反応速度を早くさせ
るためである。The reason why the egg shell pieces after firing were finely pulverized to a powder of 1 mm or less was to ensure that the product obtained by the pulverization reaction of the obtained highly active calcium oxide was a uniform product. This is also for increasing the reaction speed of powdering.
【0036】この生成された高活性酸化カルシウムの活
性を検討すべく、高活性酸化カルシウム100gに同量
(100g、100ml)の木酢液を加入し、30秒間撹
拌し、静置した。時間の経過と共に泥状の混合物の表面
に木酢液が少し浮いてきて、静置後6分し、泥状の混合
物の表面に亀裂ができ、水分が蒸発し、微粉末のCa結
合の木酢酸粉末ができた。In order to study the activity of the produced high-activity calcium oxide, the same amount (100 g, 100 ml) of wood vinegar was added to 100 g of high-activity calcium oxide, stirred for 30 seconds and allowed to stand. The wood vinegar slightly floated on the surface of the mud-like mixture with the passage of time, and after 6 minutes of standing, cracks were formed on the surface of the mud-like mixture, water evaporated, and fine powder of Ca-bonded wood acetic acid. A powder is formed.
【0037】こうして得られた微粉末中の木酢液の成分
を調べたところ、添加された高活性酸化カルシウムと結
合した木酢液の成分と認められた。When the components of the wood vinegar solution in the fine powder thus obtained were examined, it was recognized as the components of the wood vinegar solution combined with the added highly active calcium oxide.
【0038】次に、焼成温度のみを1500℃と変え、
他はこの実施例と同様の方法で、高活性酸化カルシウム
を生成し、前記と同様に活性を検討したところ、150
0℃の高温焼成による場合でも、1300℃の高温焼成
による場合と、その活性に差異が見られず、木酢液を加
えて微粉末化させる反応速度もほぼ同等であった。そこ
で、生成する効率のよさ及び費用の観点から、焼成温度
の上限を一応1500℃と定めた。Next, only the firing temperature was changed to 1500 ° C.,
Others produced highly active calcium oxide in the same manner as in this example and examined the activity in the same manner as described above.
Even in the case of the high temperature calcination at 0 ° C., there was no difference in the activity from the case of the high temperature calcination at 1300 ° C., and the reaction rates of adding wood vinegar and making it into fine powder were almost the same. Therefore, from the viewpoint of efficiency of generation and cost, the upper limit of the firing temperature is set to 1500 ° C.
【0039】[0039]
【実施例6】いか肝油100gに、木酢液20gと、1
300℃の焼成温度で得た本願発明の高活性酸化カルシ
ウム粉末120gとを入れて、撹拌後静置したところ、
10分間で反応を終了し、230gのいか肝油微粉末が
得られた。[Example 6] 100 g of squid liver oil, 20 g of wood vinegar solution and 1
120 g of the highly active calcium oxide powder of the present invention obtained at a firing temperature of 300 ° C. was added, and the mixture was left standing after stirring,
The reaction was completed in 10 minutes, and 230 g of squid liver oil fine powder was obtained.
【0040】このいか肝油微粉末の成分を分析したとこ
ろ、下記の成分がすべて含まれており、いか肝油成分が
ほぼそのまま含まれていることが判明した。When the components of this squid liver oil fine powder were analyzed, it was found that all of the following components were contained and that the squid liver oil component was contained almost as it was.
【0041】いか肝油微粉末に含まれていた成分;ミリ
スチン酸、ペンタデカン酸、パルミチン酸、ヘキサデカ
ン酸(n−11)、ヘキサデカン酸(n−5)、パルミ
トレイン酸、ヘキサデカン酸(n−9)、ステアリン
酸、オクタデカン酸(n−5)、オクタデカン酸(n−
7)、オレイン酸、リノール酸、リノレン酸、オクタデ
カテトラエン酸(n−3)、エイコセン酸(n−1
1)、エイコセン酸(n−7)、エイコセン酸(n−
9)、エイコサジェン酸(n−6)、ジホモ−γ−リノ
レン酸、エイコサテトラエン酸(n−3)、アラキドン
酸、エイコサペンタエン酸、ドコセン酸(n−11)、
ドコセン酸(n−7)、エルシン酸、ドコサペンタエン
酸(n−3)、ドコサヘキサエン酸(n−3)、テトラ
コセン酸(n−9)Components contained in squid liver oil fine powder: myristic acid, pentadecanoic acid, palmitic acid, hexadecanoic acid (n-11), hexadecanoic acid (n-5), palmitoleic acid, hexadecanoic acid (n-9), Stearic acid, octadecanoic acid (n-5), octadecanoic acid (n-
7), oleic acid, linoleic acid, linolenic acid, octadecatetraenoic acid (n-3), eicosenoic acid (n-1)
1), eicosenoic acid (n-7), eicosenoic acid (n-
9), eicosagenic acid (n-6), dihomo-γ-linolenic acid, eicosatetraenoic acid (n-3), arachidonic acid, eicosapentaenoic acid, docosenoic acid (n-11),
Docosenoic acid (n-7), erucic acid, docosapentaenoic acid (n-3), docosahexaenoic acid (n-3), tetracosenoic acid (n-9)
【0042】従来、粉末酸化カルシウムと液状油脂類の
みでは化学反応を起こすことがなく、液状油脂類が単に
粉末酸化カルシウムに吸収されるにすぎないので、油脂
の粘着性はそのまま保存され、粘着性のない油脂類の粉
末を生成することはできなかった。しかし、この実施例
のように、本願発明の高活性酸化カルシウムを用いれ
ば、粘着性のない油脂類の粉末を容易に生成できたので
ある。また、この粉末化は、油脂類と高活性酸化カルシ
ウムおよび木酢液とを単に混合させるのみで化学反応さ
せるので、従来行われていたような、積極的加工(例え
ば、ミキシング、加温、その他)は必要なかった。Conventionally, powdered calcium oxide and liquid oils and fats alone do not cause a chemical reaction, and liquid oils and fats are simply absorbed by powdered calcium oxides. No oily fat powder could be produced. However, as in this Example, the use of the highly active calcium oxide of the present invention made it possible to easily produce a powder of oils and fats having no stickiness. In addition, this powdering causes a chemical reaction by simply mixing oils and fats with highly active calcium oxide and wood vinegar, so that active processing (eg, mixing, heating, etc.), which is conventionally performed, is performed. Was not needed.
【0043】[0043]
【実施例7】天プラ油100gに、1200℃の焼成温
度で得た本願発明の高活性酸化カルシウム粉末120g
と、水20gとを容器に入れ、軽く撹拌した後、放置し
たところ、6分間で、天プラ油微粉末230gができ
た。Example 7: 120 g of highly active calcium oxide powder of the present invention obtained at a firing temperature of 1200 ° C. in 100 g of oil of heaven
Then, 20 g of water and 20 g of water were put in a container, stirred lightly, and left to stand, and 230 g of fine powder of top-grade oil was formed in 6 minutes.
【0044】[0044]
【実施例8】天プラ油100gに、1200℃の焼成温
度で得た本願発明の高活性酸化カルシウム粉末120g
と、木酢液20gとを容器に入れ、軽く撹拌した後、放
置したところ、3分間で、天プラ油微粉末230gがで
きた。[Embodiment 8] 120 g of highly active calcium oxide powder of the present invention obtained at a firing temperature of 1200 ° C. in 100 g of plastic oil
Then, 20 g of wood vinegar was placed in a container, stirred lightly, and allowed to stand, and 230 g of fine powder of top-grade plastic oil was formed in 3 minutes.
【0045】実施例7、8から明らかなように、液状油
脂と本願発明の高活性酸化カルシウムとの反応に水ある
いは木酢液のどちらを加えても油脂を粉末化することが
できるが、木酢液を加えたほうが、粉末化反応は速かっ
た。これは、一般に炭素の数の多い脂肪酸や、そのエス
テル化合物は、水に対してよりも、有機溶媒あるいは有
機物質を含む溶液(例えば、木酢液)によく溶けるの
で、木酢液を使用した場合には、水を使用した場合より
も粉末化する反応が早いものと思われる。As is clear from Examples 7 and 8, the oil and fat can be powdered by adding either water or wood vinegar to the reaction between the liquid oil and fat and the highly active calcium oxide of the present invention. The powdering reaction was faster with the addition of. This is because fatty acids with a large number of carbon atoms and their ester compounds generally dissolve better in an organic solvent or a solution containing an organic substance (for example, wood vinegar) than in water. Appears to have a faster powdering reaction than when water is used.
【0046】また、以上の実施例1〜8より、本願発明
で得られた高活性酸化カルシウムは含水物を微粉末化さ
せるという活性を有しており、粉末化剤として有用であ
る事が判明した。Further, from the above Examples 1 to 8, it was found that the highly active calcium oxide obtained in the present invention has an activity of finely pulverizing a water-containing substance and is useful as a powdering agent. did.
【0047】[0047]
【対照例1】水洗した白色卵殻を自然乾燥し、この卵殻
片を電気炉で通風雰囲気化(80cm3 / min)において
800℃で5時間焼成し、その後、自然冷却させた。こ
うして得た焼成処理後の白色卵殻片を微粉砕し、1mm以
下の粉末にしてカルシウムを得た。[Comparative Example 1] White eggshells washed with water were naturally dried, and the eggshell pieces were fired in an electric furnace at 800 ° C for 5 hours in a ventilated atmosphere (80 cm 3 / min), and then naturally cooled. The thus-calcined white eggshell pieces were finely pulverized into powder of 1 mm or less to obtain calcium.
【0048】この生成されたカルシウムの活性を検討す
べく、カルシウムに同重量の木酢液を加入し、30秒間
撹拌し、静置した。この場合にガスが発生し、臭いがす
るとともに、泡立ちが見られた。その後24時間経過し
ても木酢液とカルシウムとが分離したままで、粉末化は
できなかった。In order to examine the activity of the produced calcium, the same weight of wood vinegar solution was added to calcium, and the mixture was stirred for 30 seconds and allowed to stand. In this case, gas was generated, smelled, and bubbling was observed. Even after the lapse of 24 hours, the wood vinegar and calcium were still separated and could not be pulverized.
【0049】この対照例1より、焼成温度が800℃の
場合には、活性不足のために、得られたカルシウムを木
酢液と混合した場合に、当該木酢液を微粉末化させるこ
とはできないことが判明した。From Comparative Example 1, when the firing temperature is 800 ° C., the wood vinegar solution cannot be made into a fine powder when the obtained calcium is mixed with wood vinegar solution due to lack of activity. There was found.
【0050】[0050]
【対照例2】石灰石を900℃で5時間焼成した生石灰
(足立石灰工業製造の酸化カルシウム)を粉砕し、これ
を同重量の木酢液に投入したところ、瞬間的に発熱反応
を生じ、水分が蒸発した。しかしながら、粉末化した部
分と、固形化した部分との不均一混合物となった。固形
化部分は泡状の結合固形となり、やや褐色に変色し、全
体としては均一な微粉末化はできなかった。[Comparative Example 2] Quick lime (calcium oxide manufactured by Adachi lime Industry Co., Ltd.) obtained by firing limestone at 900 ° C for 5 hours was crushed and added to the same weight of wood vinegar solution, whereupon an exothermic reaction instantaneously occurred and the water content changed. Evaporated. However, it resulted in a heterogeneous mixture of powdered and solidified parts. The solidified portion became a bubble-like bonded solid and turned a little brown, and uniform fine powder could not be obtained as a whole.
【0051】したがって、本願発明によって得られる高
活性酸化カルシウムと木酢液との反応は、既知の生石灰
(CaO)と木酢液との反応とは全く異なり、木酢液を
その成分を性状変性させることなく、かつ微粉末化させ
ることのできる、前例のない化学変化であることが、こ
の対照例2より明らかになった。Therefore, the reaction between the highly active calcium oxide obtained by the present invention and the wood vinegar solution is completely different from the reaction between known quick lime (CaO) and wood vinegar solution, and the properties of the wood vinegar solution are not modified. It was revealed from this control example 2 that it is an unprecedented chemical change that can be made into a fine powder.
【0052】[0052]
【実験例1】本願発明で得た高活性酸化カルシウムと他
のカルシウムとを、その導電率、カルシウム粉末の色、
木酢液との粉末化反応について検討したところ、以下の
結果を得た。[Experimental Example 1] The high activity calcium oxide obtained in the present invention and other calcium were evaluated for their conductivity, color of calcium powder,
When the powdering reaction with wood vinegar was examined, the following results were obtained.
【0053】なお、この実験には、1300℃と、90
0℃の焼成温度で得た本願発明の高活性酸化カルシウ
ム、カキ殻を1300℃と、900℃の焼成温度で得た
カキ殻カルシウム、生石灰(足立石灰工業製)、試薬用
酸化カルシウム(和光純薬製)を用いた。In this experiment, 1300 ° C. and 90
Highly active calcium oxide of the present invention obtained at a calcination temperature of 0 ° C, oyster shell calcium at 1300 ° C and oyster shell calcium obtained at a calcination temperature of 900 ° C, quicklime (manufactured by Adachi Lime Industry), calcium oxide for reagents (Wako Pure) (Medicinal product) was used.
【0054】導電率について 導電率とは導体中での電流の流れ易さを示す指標を意味
する。この実験では、精製水に1/10000の各種カ
ルシウムをそれぞれ溶かし、イオン伝導に基づく導電率
を測定した。その数値の大きさにより、各種カルシウム
のイオン化率の違いを判断した。現在の栄養学ではカル
シウムはイオン化しないと吸収されないことがわかって
いる。そこで、各種カルシウムのイオン化状態を導電率
の測定によって判断した。実験によれば、1300℃の
焼成温度で得た本願発明の高活性酸化カルシウムが最も
導電率が高く、すなわちイオン化率が高いことがわかっ
た。従って、1300℃の焼成温度で得た本願発明の高
活性酸化カルシウムが、1300℃の焼成温度で得たカ
キ殻カルシウム、その他のカルシウムに比べて、生体内
(家畜などの体内)で、吸収されやすく、働きが高い状
態にあることがわかる。Regarding Electric Conductivity The electric conductivity means an index showing the ease of current flow in the conductor. In this experiment, 1/10000 of each kind of calcium was dissolved in purified water, and the conductivity based on ionic conduction was measured. The difference in the ionization rate of each calcium was judged based on the magnitude of the numerical value. Current nutrition studies show that calcium must be ionized before it can be absorbed. Therefore, the ionization state of each calcium was determined by measuring the conductivity. Experiments revealed that the highly active calcium oxide of the present invention obtained at a firing temperature of 1300 ° C. has the highest conductivity, that is, the ionization rate. Therefore, the highly active calcium oxide of the present invention obtained at the calcination temperature of 1300 ° C. is absorbed in the living body (in the body of livestock etc.) as compared with the oyster shell calcium and other calcium obtained at the calcination temperature of 1300 ° C. It is easy to see that it is in a high working state.
【0055】カルシウム粉末の色について 各種カルシウム粉末の色を目視にて観察、比較した。本
願発明の高活性酸化カルシウムは白色であるが、カキ殻
カルシウムは薄いクリーム色を呈している。また、生石
灰、試薬用酸化カルシウムも白色であるが、生石灰は本
願発明の高活性酸化カルシウムや試薬用酸化カルシウム
と比較するとわずかに黒っぽく見える。Color of Calcium Powder The colors of various calcium powders were visually observed and compared. The highly active calcium oxide of the present invention is white, while the oyster shell calcium has a light cream color. In addition, quick lime and calcium oxide for reagents are also white, but quick lime looks slightly darker than the highly active calcium oxide and calcium oxide for reagents of the present invention.
【0056】木酢液の粉末化について 粉末化という点から見ると、本願発明の高活性酸化カル
シウムと試薬用酸化カルシウムは、均一な粉末を生成す
ることができたが、他のカルシウムでは均一な粉末を生
成することはできなかった。Regarding pulverization of wood vinegar, from the viewpoint of pulverization, the highly active calcium oxide of the present invention and the reagent calcium oxide were able to produce a uniform powder, but other calcium gave a uniform powder. Could not be generated.
【0057】この実験の結果を表に示すと以下の通りに
なる。The results of this experiment are shown in the table below.
【0058】[0058]
【表1】 [Table 1]
【0059】[0059]
【実験例2】1300℃の焼成温度で得た本願発明の高
活性酸化カルシウムと、生石灰(足立石灰工業製)(C
aO 98%)、試薬用酸化カルシウム(和光純薬製)
(CaO 99.9%)を用いて、ラットにおけるヒマ
シ油下痢モデルに対する抗下痢効果を調べた。[Experimental Example 2] Highly active calcium oxide of the present invention obtained at a calcination temperature of 1300 ° C. and quick lime (manufactured by Adachi lime industry) (C
aO 98%), calcium oxide for reagents (manufactured by Wako Pure Chemical Industries)
(CaO 99.9%) was used to investigate the anti-diarrheal effect on the castor oil diarrhea model in rats.
【0060】SLC:SD雄性ラットそれぞれ4匹(4
週令、体重 100g〜150g)に前記三種類のCa
Oを以下の表に示すように10mg/kg、30mg/kg、1
00mg/kgを経口投与し、またコントロールとして生理
食塩水を経口投与し、30分後にヒマシ油1mlを経口投
与し、そして、次の式に基づいて、各投与量におけるそ
れぞれの抗下痢効果を判断した。SLC: SD 4 male rats each (4
Weekly, body weight 100g to 150g)
O as shown in the table below: 10 mg / kg, 30 mg / kg, 1
Oral administration of 00 mg / kg, oral administration of physiological saline as a control, and 30 minutes later, oral administration of 1 ml of castor oil, and determination of each antidiarrheal effect at each dose based on the following formula did.
【0061】[0061]
【数1】 [Equation 1]
【0062】測定値及び抗下痢指標を以下の表2に示
す。The measured values and the anti-diarrhea index are shown in Table 2 below.
【0063】[0063]
【表2】 [Table 2]
【0064】上記の表に現されるこの実験の結果、総て
のCaOについて抗下痢効果が確認されたが、鉱物に由
来する生石灰、試薬用酸化カルシウムに比して、卵殻と
いう生体に由来する本願発明の高活性酸化カルシウムが
最も強い抗下痢効果を有し、特に100mg/kg投与区で
は、2時間以内では下痢は全く発症しなかった。As a result of this experiment shown in the above table, the anti-diarrhea effect was confirmed for all CaO, but it was derived from the living body called egg shell as compared with quick lime derived from minerals and calcium oxide for reagents. The highly active calcium oxide of the present invention has the strongest antidiarrheal effect, and in the 100 mg / kg administration group, diarrhea did not occur at all within 2 hours.
【0065】[0065]
【発明の効果】本願発明で得られる高活性酸化カルシウ
ムは、水分が加えられることによって、急速に反応し、
微粉末化する。また、この高活性酸化カルシウムは含水
物を微粉末化させるという高活性を有しているので、粉
末化剤として有用である。The highly active calcium oxide obtained in the present invention reacts rapidly when water is added,
Micronize. Further, since this highly active calcium oxide has a high activity of making a water-containing substance into a fine powder, it is useful as a powdering agent.
【0066】前記の微粉末化は、水分のみでもよいが、
酸性水(例えば木酢液など)を加えるほうが、より急激
な反応が見られる。この高活性酸化カルシウム及び当該
高活性酸化カルシウムからなる粉末化剤は、特に血液な
どの粘性液体、あるいは、動物油脂、植物油脂、鉱物油
脂などの液状油脂類の粉末化には顕著に有効である。ま
た、混合された含水物の溶解成分を損なうことなく、か
つ当該含水物の溶解成分を性状変性させることなく微粉
末化させることができる。したがって、微粉末化するこ
とが困難な液状物質を有効成分を保有させたまま粉末化
させるについては、多大の効果がある。この微粉末化反
応は、反応熱を生じるのみであって、乾燥その他の操作
を加える必要はない。The above fine powder formation may be performed only with water,
A more rapid reaction can be seen by adding acidic water (such as wood vinegar). The highly active calcium oxide and the powdering agent composed of the highly active calcium oxide are remarkably effective for powdering viscous liquids such as blood, or liquid oils and fats such as animal oils, vegetable oils and mineral oils. . In addition, it is possible to make fine powder without damaging the dissolved components of the mixed hydrous material and without modifying the properties of the dissolved components of the hydrous material. Therefore, there is a great effect in pulverizing a liquid substance that is difficult to be pulverized while retaining the active ingredient. This pulverization reaction only generates heat of reaction and does not require drying or other operations.
Claims (4)
得た高活性酸化カルシウム。1. A highly active calcium oxide obtained by firing egg shells at 900 ° C to 1500 ° C.
て得た高活性酸化カルシウム。2. Highly active calcium oxide obtained by firing egg shells at 1200 ° C. to 1300 ° C.
得た高活性酸化カルシウムからなる粉末化剤。3. A powdering agent comprising highly active calcium oxide obtained by firing egg shells at 900 ° C. to 1500 ° C.
て得た高活性酸化カルシウムからなる粉末化剤。4. A powdering agent comprising highly active calcium oxide obtained by firing egg shells at 1200 ° C. to 1300 ° C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6021439A JPH0717711A (en) | 1993-02-24 | 1994-02-18 | Highly active calcium oxide and powdering agent |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5946893 | 1993-02-24 | ||
| JP5-59468 | 1993-02-24 | ||
| JP6021439A JPH0717711A (en) | 1993-02-24 | 1994-02-18 | Highly active calcium oxide and powdering agent |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0717711A true JPH0717711A (en) | 1995-01-20 |
Family
ID=26358500
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6021439A Pending JPH0717711A (en) | 1993-02-24 | 1994-02-18 | Highly active calcium oxide and powdering agent |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0717711A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000072685A1 (en) * | 1999-05-31 | 2000-12-07 | Houzawa, Hiromi | Method for producing bactericide |
| JP2008113661A (en) * | 2006-11-06 | 2008-05-22 | Hatsuyu Ryu | Method for producing calcium powder of ozone egg shell |
| JP2009234807A (en) * | 2008-03-25 | 2009-10-15 | Yamagata Three Top:Kk | Shell calcium powder and method for producing the same |
| CN102225780A (en) * | 2011-04-19 | 2011-10-26 | 上海彭浦冶金辅料有限公司 | High-activity calcium oxide and production method thereof |
| KR101234268B1 (en) * | 2009-10-27 | 2013-02-18 | 김일광 | Feedstuff additive comprising refined wood vinegar, calcined egg-shell, loess powder and garlic powder |
| JP2014518537A (en) * | 2011-03-25 | 2014-07-31 | キョンウォン パク | Method for producing precipitated calcium carbonate using avian eggshell |
| US8859010B2 (en) * | 2003-05-29 | 2014-10-14 | Biosynergy, Inc. | Method of producing eggshell powder |
-
1994
- 1994-02-18 JP JP6021439A patent/JPH0717711A/en active Pending
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000072685A1 (en) * | 1999-05-31 | 2000-12-07 | Houzawa, Hiromi | Method for producing bactericide |
| US8859010B2 (en) * | 2003-05-29 | 2014-10-14 | Biosynergy, Inc. | Method of producing eggshell powder |
| JP2008113661A (en) * | 2006-11-06 | 2008-05-22 | Hatsuyu Ryu | Method for producing calcium powder of ozone egg shell |
| JP2009234807A (en) * | 2008-03-25 | 2009-10-15 | Yamagata Three Top:Kk | Shell calcium powder and method for producing the same |
| KR101234268B1 (en) * | 2009-10-27 | 2013-02-18 | 김일광 | Feedstuff additive comprising refined wood vinegar, calcined egg-shell, loess powder and garlic powder |
| JP2014518537A (en) * | 2011-03-25 | 2014-07-31 | キョンウォン パク | Method for producing precipitated calcium carbonate using avian eggshell |
| CN102225780A (en) * | 2011-04-19 | 2011-10-26 | 上海彭浦冶金辅料有限公司 | High-activity calcium oxide and production method thereof |
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