JPH0446197B2 - - Google Patents

Info

Publication number
JPH0446197B2
JPH0446197B2 JP5025685A JP5025685A JPH0446197B2 JP H0446197 B2 JPH0446197 B2 JP H0446197B2 JP 5025685 A JP5025685 A JP 5025685A JP 5025685 A JP5025685 A JP 5025685A JP H0446197 B2 JPH0446197 B2 JP H0446197B2
Authority
JP
Japan
Prior art keywords
granules
water
paraffin
activated carbon
minerals
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.)
Expired
Application number
JP5025685A
Other languages
Japanese (ja)
Other versions
JPS61212383A (en
Inventor
Tomotoshi Wada
Shinobu Yamanaka
Keikichi Sato
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.)
Kunimine Industries Co Ltd
Original Assignee
Kunimine Industries 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 Kunimine Industries Co Ltd filed Critical Kunimine Industries Co Ltd
Priority to JP5025685A priority Critical patent/JPS61212383A/en
Publication of JPS61212383A publication Critical patent/JPS61212383A/en
Publication of JPH0446197B2 publication Critical patent/JPH0446197B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】[Detailed description of the invention]

(産業上の利用分野) 本発明は含有有効成分を水中で微量ずつ安定
的、継続的に放出するようにした粒剤に関し、例
えば、浄水器などに充填して飲料水に不足のビタ
ミン、ミネラル等を補給できるようにする徐放性
粒剤に関する。 (従来の技術) 浄水器等にゴミの除去、脱臭、脱色等の目的で
活性炭が一般に用いられているがこの浄化と同時
に飲料水にビタミン、ミネラル等を添加できれ
ば、健康飲料水を作ることができ好ましい。その
場合浄水器の活性炭にビタミン、ミネラル等を混
合することが考えられるが、一時に大量が溶出し
てしまい、長期間継続的、安定的に溶出するよう
にさせるのは困難である。 (発明が解決しようとする問題点) そこで、ビタミン、ミネラルを適当な無機塩と
混合しこれをポリビニルアルコールをバインダー
として粒状に成形することも試みられた。しかし
ながら、この粒状物においても、溶出速度を制御
することは困難であつた。例えば粒剤は水中にお
いて吸収して亀裂を生じしばしば崩壊してしまう
が、一方崩壊を防ぐためにバインダーの量を増し
水中における強度を上げると有効物質の溶出速度
が低下してしまう。 (問題点を解決するための手段) 本発明者らはこのような粒剤混入成分の微量放
出コントロールに主眼をおき、鋭意研究を進めた
結果、意外にも、ビタミン、ミネラル等を活性炭
粉末と混合し、これを酢酸ビニル樹脂液をバイン
ダーとして造粒したものはパラフインにて表面コ
ーテイングをすることにより、それが粒剤の内部
に吸収されて、広範囲で正確、かつ、安定継続的
な放出が行われるように長期的なコントロールが
可能な粒剤が得られることを見出し、本発明を完
成するに至つた。 すなわち本発明は、活性炭粉末と各種ビタミ
ン、ミネラル等(以下、単にミネラル等という)
の粉末の混合物を樹脂バインダーを用いて造粒
し、パラフインを含浸してなることを特徴とする
水中徐放性粒剤を提供するものである。 本発明において活性炭粉末の種類に特に制限は
ない。粉末は細かければ細かいほど良いが通常4
〜250メツシユ(4.76〜0.063mm)の大きさのもの
が用いられる。 また、活性炭には、50重量%までの範囲で、リ
ン酸水素カルシウム、炭酸カルシウム、アルミナ
などを混合してもよい。 また、ミネラル等とは、通常のミネラルの他、
その他の水中溶出性の各種化合物を包含する意味
であり例えば有機ゲルマニウム、カルシウム、ナ
トリウム化合物、ビタミンC、ビタミンD、ビタ
ミンEなどをあげることができる。 活性炭粉末に対するミネラル等の割合は、最大
で1:1である。ミネラル等の量が活性炭とミネ
ラル等との合計量の50重量%以上では、水中での
溶出量の制御が困難ないしは不可能となる。また
1重量%以下では、長期にわたる十分な溶出量が
得られない。 樹脂バインダーとしては、ポリビニルホルマー
ル、ポリメタクリル酸メチル、ポリ塩化ビニルな
どがあるが、酢酸ビニル樹脂又はエチレン、スチ
レン、アクリレート、メタクリレートなどと共重
合した酢酸ビニルエマルジヨンが好ましく用いら
れる。これを溶剤中に分散して用いる。溶剤とし
てはエタノールが好ましく用いられる。 バインダーの量は、活性炭100重量部に対し、
通常5〜50重量部、好ましくは10〜30重量部用い
られる。5重量部未満では造粒性が極めて低下
し、また、できた造粒品の機械的強度が不足し、
粒剤が水中で崩壊してしまう。バインダーは多い
程機械的強度が増すが50重量部を越えると、活性
炭の多孔性が低減し、パラフインを吸収する表面
が不足してしまう。 造粒は常法を採用することができ、例えば押出
し法、転動法、流動法などがある。粒子の大きさ
は0.3mm〜10mmの範囲とするのが好ましい。 粒状物へのパラフインの含浸はパラフインを加
温し、これを表面コーテイングする方法より行う
ことができる。 パラフインの塗布量は、粒状物100重量部に対
し通常10〜40重量部、好ましくは20〜30重量部で
ある。パラフインが15重量部未満では、有効物質
の溶出を制御できず、数週間で溶出しつくしてし
まい、初期溶出濃度が著しく高くなる。また40重
量部を越えると溶出が極めて微小となるかまたは
溶出が起きない場合が生じる。 本発明においてパラフインはコーテイング直後
は表面にあるが、一定時間経過後は少なくとも一
部は、粒状物の活性炭が多孔質であるので粒状物
の内部へ吸収されることが必要である。パラフイ
ンとしては食品包装紙の被覆に用いられているも
のが好ましい。 本発明は、活性炭粉末、樹脂バインダー、パラ
フインとの割合を微妙にバランスさせることによ
り、活性炭の粒状物の機械的強度を保持すると共
に多孔質部分を保持させ、多孔性部分の表面にパ
ラフインを含浸させて、その多孔質部分の割合を
制御しミネラル等の溶出量を制御することに特徴
がある。 本考案の水中徐放性粒剤は、例えば水100重量
部に対し、粒剤1〜30重量部、1日の使用水量
3.0の条件で0.1〜100ppmの範囲で制御して、
安定的に1ケ月以上継続的にミネラル等を放出さ
せる。 (発明の効果) 本発明の粒剤はミネラル等を含有し、機械的強
度にすぐれる粒剤であり、水中でそれらを徐々に
放出し、長期間、安定的に飲料水中にミネラル等
を補給する粒剤として好適である。 また、基材として活性炭を用い、本発明の粒剤
は無害であるばかりでなく、脱臭、脱色等の水浄
化機能を有する。 (実施例) 次に本発明を実施例に基づきさらに詳細に説明
する。なお実施例中、特にことわらない限り、%
は重量%を示す。 実施例 1 活性炭950gとゲルマニウム原体50gを混合し
た。(ゲルマニウム原体としては のものを用いた。)次いでこの混合物に酢酸ビニ
ル樹脂溶液100ml(固型分18.5重量%)を添加し
たのち、これを混練造粒して粒径約2mmの粒状物
を調製した。 この粒状物に次のようにしてパラフインを20
%、30%、40%及び50%塗布して試料No.2、3、
4及び5を製造した。流動乾燥器内にパラフイン
粉末と粒状物を入れ、上昇熱風中、約70℃で攪拌
し、溶融パラフインを粒状物に塗布し、含浸させ
た。また、パラフインを塗布しない粒状物を試料
No.1とした。 この粒剤試料No.1〜5をそれぞれ10gとり、そ
れを300ml容三角フラスコにそれぞれ入れ、水250
mlを加え25℃保温槽の中に放置した。こうして
1,2,6,24,48時間の経過後において1mlず
つ採水し、その濃度を測定した。この結果を第1
図に示した。 同図の結果よりパラフインの塗布量により大き
く溶出量が変化し溶出速度を任意に設定できるこ
とがわかる。 実施例 2 活性炭粉末900gに対し、ゲルマニウム原体100
gを用いた以外は実施例1と同様にして粒状物を
調製し、実施例1と同様にして、パラフイン塗布
量30%、35%及び40%の粒剤を製造した。 この試料をカラムの大きさ、径80mm、長さ110
mmの円筒に充填し、粒状活性炭130g、本粒剤30
g、ろ過水3/分、4時間経過ごとに500mlず
つ採水し溶出量を測定した。この結果を第1表に
示した。なお水のPHは約7.2と試験開始時と終了
後でほとんど変動しなかつた。
(Industrial Application Field) The present invention relates to granules that stably and continuously release the active ingredients contained in water little by little. The present invention relates to a sustained release granule that enables the replenishment of such substances. (Prior art) Activated carbon is generally used in water purifiers for the purpose of removing dust, deodorizing, decolorizing, etc. If vitamins, minerals, etc. can be added to drinking water at the same time as purification, it would be possible to create healthy drinking water. It's good to be able to do it. In this case, it may be possible to mix vitamins, minerals, etc. with the activated carbon in the water purifier, but a large amount of them would be eluted at once, and it would be difficult to make them elute continuously and stably for a long period of time. (Problems to be Solved by the Invention) Therefore, attempts have been made to mix vitamins and minerals with appropriate inorganic salts and mold the mixture into granules using polyvinyl alcohol as a binder. However, even in this granular material, it was difficult to control the elution rate. For example, granules absorb into water, crack and often disintegrate, but on the other hand, if the amount of binder is increased to increase the strength in water to prevent disintegration, the elution rate of the active substance will be reduced. (Means for Solving the Problems) The present inventors focused on controlling the release of small amounts of ingredients mixed in granules, and as a result of intensive research, we unexpectedly discovered that vitamins, minerals, etc. can be mixed with activated carbon powder. The mixture is mixed and granulated using vinyl acetate resin liquid as a binder. By coating the surface with paraffin, it is absorbed into the inside of the granules, allowing accurate, stable and continuous release over a wide range. The present inventors have discovered that it is possible to obtain granules that can be controlled over a long period of time, and have completed the present invention. That is, the present invention provides activated carbon powder and various vitamins, minerals, etc. (hereinafter simply referred to as minerals, etc.).
The present invention provides sustained-release granules in water, which are obtained by granulating a powder mixture using a resin binder and impregnating it with paraffin. In the present invention, there is no particular restriction on the type of activated carbon powder. The finer the powder, the better, but usually 4
The size of ~250 mesh (4.76 ~ 0.063 mm) is used. Further, activated carbon may be mixed with calcium hydrogen phosphate, calcium carbonate, alumina, etc. in an amount up to 50% by weight. In addition to normal minerals, minerals etc.
The term includes various other water-soluble compounds, such as organic germanium, calcium, sodium compounds, vitamin C, vitamin D, and vitamin E. The ratio of minerals, etc. to activated carbon powder is at most 1:1. If the amount of minerals, etc. exceeds 50% by weight of the total amount of activated carbon and minerals, etc., it becomes difficult or impossible to control the amount of elution in water. Moreover, if it is less than 1% by weight, a sufficient amount of elution cannot be obtained for a long period of time. Examples of the resin binder include polyvinyl formal, polymethyl methacrylate, and polyvinyl chloride, but vinyl acetate resin or vinyl acetate emulsion copolymerized with ethylene, styrene, acrylate, methacrylate, etc. is preferably used. This is used by dispersing it in a solvent. Ethanol is preferably used as the solvent. The amount of binder is 100 parts by weight of activated carbon.
Usually 5 to 50 parts by weight, preferably 10 to 30 parts by weight are used. If it is less than 5 parts by weight, the granulation property will be extremely reduced, and the mechanical strength of the resulting granulated product will be insufficient.
Granules disintegrate in water. The mechanical strength increases as the amount of binder increases, but if it exceeds 50 parts by weight, the porosity of the activated carbon decreases, resulting in a lack of surface area for absorbing paraffin. Conventional methods can be used for granulation, such as an extrusion method, a rolling method, and a fluidization method. Preferably, the particle size is in the range of 0.3 mm to 10 mm. Impregnation of paraffin into granules can be carried out by heating paraffin and coating the surface thereof. The amount of paraffin applied is usually 10 to 40 parts by weight, preferably 20 to 30 parts by weight, per 100 parts by weight of the granules. If the paraffin is less than 15 parts by weight, the elution of the effective substance cannot be controlled, and it will be completely eluted within several weeks, resulting in a significantly high initial elution concentration. If the amount exceeds 40 parts by weight, elution may be extremely small or no elution may occur. In the present invention, the paraffin is present on the surface immediately after coating, but after a certain period of time, at least a portion of the paraffin needs to be absorbed into the inside of the granules because the activated carbon in the granules is porous. As the paraffin, those used for coating food wrapping paper are preferred. The present invention maintains the mechanical strength of activated carbon granules and retains the porous portion by delicately balancing the ratio of activated carbon powder, resin binder, and paraffin, and impregnates the surface of the porous portion with paraffin. It is characterized by controlling the proportion of the porous portion and controlling the amount of minerals etc. eluted. The sustained release granules in water of the present invention can be prepared by using, for example, 1 to 30 parts by weight of the granules per 100 parts by weight of water, and the amount of water used per day.
Controlled in the range of 0.1 to 100ppm under the condition of 3.0,
Minerals, etc. are released stably and continuously for more than one month. (Effects of the Invention) The granules of the present invention contain minerals, etc. and have excellent mechanical strength, and gradually release them into water, stably replenishing minerals, etc. into drinking water over a long period of time. It is suitable as a granule. Moreover, the granules of the present invention using activated carbon as a base material are not only harmless but also have water purification functions such as deodorization and decolorization. (Examples) Next, the present invention will be described in more detail based on Examples. In the examples, unless otherwise specified, %
indicates weight %. Example 1 950 g of activated carbon and 50 g of germanium raw material were mixed. (As a germanium raw material, I used the one from ) Next, 100 ml of vinyl acetate resin solution (solid content: 18.5% by weight) was added to this mixture, and this was kneaded and granulated to prepare granules with a particle size of about 2 mm. Add paraffin to this granule for 20 minutes as follows:
%, 30%, 40% and 50% and sample No. 2, 3,
4 and 5 were produced. Paraffin powder and granules were placed in a fluidized fluid dryer and stirred at about 70°C in rising hot air to coat and impregnate the molten paraffin onto the granules. In addition, samples of granular materials without paraffin applied
It was ranked No.1. Take 10g of each of these granule samples No. 1 to 5, put them into 300ml Erlenmeyer flasks, and add 250g of water.
ml was added and left in a 25°C heat insulating tank. After 1, 2, 6, 24, and 48 hours had elapsed, 1 ml of water was sampled and its concentration was measured. This result is the first
Shown in the figure. The results shown in the figure show that the elution amount changes greatly depending on the amount of paraffin applied, and the elution rate can be set arbitrarily. Example 2 100 g of germanium raw material for 900 g of activated carbon powder
Granules were prepared in the same manner as in Example 1, except that g was used, and granules with paraffin coating amounts of 30%, 35% and 40% were produced in the same manner as in Example 1. Column size: 80 mm diameter, 110 mm length
Filled into a mm cylinder, 130g of granular activated carbon, 30g of this granule
g, filtered water at 3/min, and 500 ml of water was sampled every 4 hours to measure the amount of elution. The results are shown in Table 1. The pH of the water was approximately 7.2, which hardly changed between the start and end of the test.

【表】【table】

【表】 実施例 3 活性炭粉末990gに対しゲルマニウム原体10g
を用いた以外は実施例2の試料No.1と同様にして
パラフインを30%塗布して粒剤を調製し、それを
実施例2と同様にしてカラムに充填し、ゲルマニ
ウム原体の溶出量を測定した。その結果を第2表
に示した。同表の結果より、Ge原体が1%と、
実施例2の試料No.1に比べ1/10になつても、その
溶出量は比較的多く、かつ、安定していることが
わかる。
[Table] Example 3 10g of germanium raw material for 990g of activated carbon powder
A granule was prepared by applying 30% paraffin in the same manner as Sample No. 1 of Example 2, except that granules were used, and the granules were packed into a column in the same manner as in Example 2. was measured. The results are shown in Table 2. From the results in the same table, the Ge base material is 1%.
It can be seen that even though it is 1/10 compared to sample No. 1 of Example 2, the elution amount is relatively large and stable.

【表】【table】

【表】【table】

【表】【table】 【図面の簡単な説明】[Brief explanation of the drawing]

第1図は実施例1の粒剤の水中におけるゲルマ
ニウム分の溶出量と時間との関係を示すグラフで
ある。
FIG. 1 is a graph showing the relationship between the elution amount of germanium in water from the granules of Example 1 and time.

Claims (1)

【特許請求の範囲】[Claims] 1 活性炭粉末と各種ビタミン、ミネラル等の粉
末の混合物を樹脂バインダーを用いて造粒し、パ
ラフインを含浸させてなることを特徴とする水中
徐放性粒剤。
1. A sustained-release granule in water, which is made by granulating a mixture of activated carbon powder and powders of various vitamins, minerals, etc. using a resin binder and impregnating it with paraffin.
JP5025685A 1985-03-15 1985-03-15 Granule slowly releasable in water Granted JPS61212383A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5025685A JPS61212383A (en) 1985-03-15 1985-03-15 Granule slowly releasable in water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5025685A JPS61212383A (en) 1985-03-15 1985-03-15 Granule slowly releasable in water

Publications (2)

Publication Number Publication Date
JPS61212383A JPS61212383A (en) 1986-09-20
JPH0446197B2 true JPH0446197B2 (en) 1992-07-29

Family

ID=12853896

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5025685A Granted JPS61212383A (en) 1985-03-15 1985-03-15 Granule slowly releasable in water

Country Status (1)

Country Link
JP (1) JPS61212383A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5055005B2 (en) * 2007-04-12 2012-10-24 智里 大丸 Hydrogen-rich water production method and hydrogen-rich water generator

Also Published As

Publication number Publication date
JPS61212383A (en) 1986-09-20

Similar Documents

Publication Publication Date Title
US4366310A (en) Controlled release compositions
CA2489318C (en) Adsorbent of latent-heat storage type for canister and process for producing the same
JP2558023B2 (en) Method for producing active element granules by extrusion
JP5951950B2 (en) Method for treating contaminated water containing radioactive substance and method for adjusting particle size of radioactive substance removing agent
DE3208672C2 (en)
JPS56140915A (en) Pharmaceutical preparation for solid drug
DE2040297B2 (en) Process for the production of a shaped body which is adsorptive for gases and liquids
US5030391A (en) Process for the production of spherical particles of ceramics
US4267138A (en) Coating ensuring a controlled release of active ingredients of biologically active compositions, particularly pharmaceutical compositions and a process for preparation of biologically active compositions ensuring controlled release of active ingredients
O'Connor et al. Drug release mechanism from a microcrystalline cellulose pellet system
DE19843887C5 (en) Hygiene granulate and process for its production
JPH0446197B2 (en)
Sprockel et al. Development of an emulsion-solvent evaporation technique for microencapsulation of drus-resin complexes
JP4797245B2 (en) Snail pesticide and method
CN109603778B (en) Cigarette filter adsorbing material, preparation method thereof and cigarette filter
JP2004300128A (en) Antibacterial carbonaceous substance
JP3602654B2 (en) Sustained release antibacterial agent
JPS6363522B2 (en)
JP2001055303A (en) Agrochemical granule having controlled release function
JPS60241930A (en) Moisture absorbent
JPS6313708B2 (en)
JPH03167124A (en) Manufacture of pellet consisting of xanthine derivative
JPH0375256A (en) Functional ceramics and production thereof
JPS6363523B2 (en)
JPS59193979A (en) Volatile composition