JP2986810B2 - Dialysis agent and method for producing the same - Google Patents

Dialysis agent and method for producing the same

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Publication number
JP2986810B2
JP2986810B2 JP1206940A JP20694089A JP2986810B2 JP 2986810 B2 JP2986810 B2 JP 2986810B2 JP 1206940 A JP1206940 A JP 1206940A JP 20694089 A JP20694089 A JP 20694089A JP 2986810 B2 JP2986810 B2 JP 2986810B2
Authority
JP
Japan
Prior art keywords
agent
dialysis
dialysis agent
component
baking soda
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 - Fee Related
Application number
JP1206940A
Other languages
Japanese (ja)
Other versions
JPH0374331A (en
Inventor
信夫 伊藤
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.)
Nikkiso Co Ltd
Original Assignee
Nikkiso 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 Nikkiso Co Ltd filed Critical Nikkiso Co Ltd
Priority to JP1206940A priority Critical patent/JP2986810B2/en
Priority to US07/564,159 priority patent/US5071558A/en
Priority to DE69018172T priority patent/DE69018172T3/en
Priority to EP90115320A priority patent/EP0417478B2/en
Priority to CA002023075A priority patent/CA2023075C/en
Publication of JPH0374331A publication Critical patent/JPH0374331A/en
Application granted granted Critical
Publication of JP2986810B2 publication Critical patent/JP2986810B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は透析用剤、特に使用時溶解したときに反応に
より沈澱物を生じず、均質で組成安定性及び流動性の良
好なように粒状化せしめ、かつそれを溶解せしめる際に
は易溶性である粒状化せしめた透析用剤に係るものであ
る。
DETAILED DESCRIPTION OF THE INVENTION [Industrial application] The present invention relates to a dialysis agent, in particular, a granular material which is free from a precipitate upon reaction when dissolved when used, is homogeneous, has good composition stability and good flowability. The present invention relates to a granulated dialysis agent which is easily soluble when it is dissolved and dissolved.

[従来の技術] 透析用剤は、透析液を作成するための薬剤である。透
析液は、人工腎臓(血液透析、腹膜透析等)などにより
本来腎臓が行なう機能に代わり、体液の老廃物を取り去
り、更には血液中に必要な成分を補うために用いるもの
であり、アルカリ化剤として重曹を用いる重曹透析液が
生理的に有効であるため注目されている。重曹透析液と
しては、以下に示すような電解質イオン組成を有するも
のが用いられている。
[Related Art] A dialysis agent is an agent for preparing a dialysate. The dialysate is used to remove the waste of body fluids and to supplement the necessary components in the blood, instead of the functions originally performed by the kidneys by artificial kidneys (hemodialysis, peritoneal dialysis, etc.). A baking soda dialysate using baking soda as an agent has attracted attention because it is physiologically effective. As the sodium bicarbonate dialysate, one having the following electrolyte ion composition is used.

Na+ 120〜150mEp/ K + 0.5〜3.0 〃 Ca++ 1.5〜4.5 〃 Mg++ 0〜2.0 〃 Cl- 90〜135 〃 CH3COO- 5〜 35 〃 HCO3 - 20〜 35 〃 ブドウ糖 0〜250g/ 普通重曹透析液は、重曹以外の必要電解質の約2.5kg
余に水を加えて溶解度の関係から約10の容積の原液A
とし、これとアルカリ剤としての重曹水溶液とに分け、
透析時に両者を混合して全量を350に希釈して用いら
れる。重曹については粉末状にて保存あるいは輸送して
使用の直前に溶解することもある。
Na + 120~150mEp / K + 0.5~3.0 〃 Ca ++ 1.5 to 4.5 〃 Mg ++ 0 to 2.0 〃 Cl - 90 to 135 〃 CH 3 COO - 5~ 35 〃 HCO 3 -. 20 to 35 〃 glucose 0 250g / normal baking soda dialysate is about 2.5kg of required electrolytes other than baking soda
About 10 volumes of stock solution A
And divided into this and an aqueous solution of sodium bicarbonate as an alkaline agent,
At the time of dialysis, both are mixed and the total amount is diluted to 350 before use. Baking soda may be stored or transported in powder form and dissolved immediately before use.

[発明の解決しようとする課題] しかしながら、前記の如く重曹水溶液と他の電解質成
分溶解を予め調製しておく場合には、これを濃厚な原液
としたにしても、かなりの容積と重量になり、貯留や運
搬に不便を来たす欠点がある。
[Problems to be Solved by the Invention] However, when the aqueous solution of sodium bicarbonate and other electrolyte components are prepared in advance as described above, even if this is a concentrated stock solution, the volume and weight become considerable. However, there is a disadvantage that storage and transportation are inconvenient.

またこれを避けるため、混合粉体として取り扱う場合
には、それぞれの粉体を構成する粒子形状や、比重が異
なる為、貯留、運搬時に成分の偏りが生じ溶解の際には
貯留単位の全量を一度に溶解しないかぎり所望の組成の
溶液が得られない。貯留単位の全量を溶かす場合におい
ても、夫々が均質に溶解せず、不均質液となり易い欠点
を有していた。あるいは、貯留時等に、重曹とカルシウ
ムまたはマグネシウム成分が反応して難溶性の炭酸塩が
生成しやすかった。
In order to avoid this, when handling as mixed powder, the particle shape and specific gravity of each powder are different, so the components are biased during storage and transportation, and the total amount of the storage unit should be reduced when dissolving. Unless the components are dissolved at once, a solution having a desired composition cannot be obtained. Even when the entire amount of the storage unit was dissolved, each had a disadvantage that they did not dissolve homogeneously and tended to become a heterogeneous liquid. Alternatively, during storage or the like, sodium bicarbonate and a calcium or magnesium component react with each other to easily generate a hardly soluble carbonate.

さらに、重曹にあっては、これを粉末にすると、一般
的に流動性が悪く、取り扱い難かったり、溶解性が悪く
なる欠点があるものと考えられてきた。
Further, in the case of baking soda, it has been considered that when it is powdered, it generally has poor fluidity, is difficult to handle, and has a disadvantage of poor solubility.

[課題を解決するための手段] 本発明は、これら従来の透析用剤が有する諸欠点を排
除し、貯留や搬送に有利であり、容易に透析液を得るこ
とのできる粉末状の透析用剤を得ることを目的としてな
されたものである。
[Means for Solving the Problems] The present invention eliminates the drawbacks of these conventional dialysis agents, is advantageous for storage and transport, and can easily obtain a dialysate. It was done with the purpose of obtaining.

本発明の構成は、以下のとおりである。 The configuration of the present invention is as follows.

(1)カルシウム成分を含み重曹を含まない群からなる
造粒物(A剤)と、重曹を含みカルシウム成分を含まな
い群からなる造粒物(B剤)との混合物であって、B剤
が塩化ナトリウム、塩化カリウム及び酢酸ナトリウムか
ら選ばれた少なくとも1種の電解質成分と重曹とからな
る均質な造粒物であり、かつA剤とB剤の粒径は平均粒
径が大きな剤の平均粒径に対する小さな剤の平均粒径の
比が0.9以上であることを特徴とする透析用剤。
(1) a mixture of a granulated product (agent A) comprising a group containing a calcium component and not containing baking soda and a granulated product (agent B) comprising a group containing baking soda and containing no calcium component, Is a homogeneous granulated product comprising at least one electrolyte component selected from sodium chloride, potassium chloride and sodium acetate and sodium bicarbonate, and the particle size of the agent A and the agent B is the average of those having a large average particle size. A dialysis agent, wherein the ratio of the average particle size of the small agent to the particle size is 0.9 or more.

(2)透析用剤の溶解速度が3分以内である前記(1)
記載の透析用剤。
(2) The above (1), wherein the dissolution rate of the dialysis agent is within 3 minutes.
The dialysis agent according to the above.

(3)透析用剤の安息角が50度以下である前記(1)又
は(2)記載の透析用剤。
(3) The dialysis agent according to the above (1) or (2), wherein the angle of repose of the dialysis agent is 50 degrees or less.

(4)塩化ナトリウム、塩化カリウム及び酢酸ナトリウ
ムから選ばれた少なくとも1種の電解質成分粉末と重曹
粉末を、水分が0.5〜15重量%となるように水を添加し
て混合し、造粒、乾燥して造粒物(B剤)を製造し、カ
ルシウム成分を含み重曹を含まない群からなる造粒物
(A剤)と混合することを特徴とする前記(1)〜
(3)のいずれか1つに記載の透析用剤の製造方法。
(4) At least one electrolyte component powder selected from sodium chloride, potassium chloride and sodium acetate and sodium bicarbonate powder are mixed by adding water so that the water content is 0.5 to 15% by weight, and granulated and dried. (1) to (1) to (4), wherein a granulated material (agent B) is produced by mixing the mixture with a granulated material (agent A) comprising a group containing a calcium component and not containing sodium bicarbonate.
The method for producing a dialysis agent according to any one of (3).

(5)前記の乾燥を、炭酸ガス雰囲気中で行うことを特
徴とする前記(4)記載の透析用剤の製造方法。
(5) The method for producing a dialysis agent according to (4), wherein the drying is performed in a carbon dioxide gas atmosphere.

本発明は、透析剤に含まれる成分をA剤とB剤の2群
に分け、それぞれを造粒した後、混合したものである。
A剤とB剤は、混合したあと容易に分級が起こらないよ
うに、造粒に当たってその粒径を制御する必要がある。
A剤とB剤の粒径は、同程度であることが好ましく、平
均粒径の大きなほうの剤の平均粒径に対する小さなほう
の剤の平均粒径の比が、0.9以上であることが好まし
い。
In the present invention, the components contained in the dialysis agent are divided into two groups, agent A and agent B, each of which is granulated and then mixed.
The particle size of the A agent and the B agent must be controlled during granulation so that classification does not easily occur after mixing.
The particle diameters of the A agent and the B agent are preferably substantially the same, and the ratio of the average particle diameter of the smaller agent to the average particle diameter of the agent having the larger average particle diameter is preferably 0.9 or more. .

本発明のB剤において、重曹と共に存在し得る成分と
しては、カルシウム成分を含まない電解質成分の一種以
上である。このような電解質成分としては、塩化ナトリ
ウム、塩化カリウム、酢酸ソーダ、塩化マグネシウムな
どが挙げられるが、その他必要に応じ、本発明の目的を
阻害しない限り例えばブドウ糖や尿素等の他の成分を適
宜併用することができる。
In the agent B of the present invention, the component that may be present together with baking soda is at least one electrolyte component that does not contain a calcium component. Examples of such an electrolyte component include sodium chloride, potassium chloride, sodium acetate, magnesium chloride, and the like. If necessary, other components such as glucose and urea are appropriately used unless the object of the present invention is inhibited. can do.

本発明のB剤は、実質的に重曹だけを含むようなもの
であってもよい。
The agent B of the present invention may be one containing substantially only baking soda.

他方A剤においては、カルシウム成分から成る電解質
成分は、これらだけ或は他の必要成分とともに造粒せし
める。このとき、A剤とB剤は分級しないような造粒物
である必要がある。通常カルシウム成分は塩化物として
調製され、造粒体の場合、CaCl2・2H2Oの形が安定して
いる。尚、更にこれらと共に酢酸やブドウ糖等の少量添
加物を所望により添加しても差し支えない。
On the other hand, in the agent A, the electrolyte component composed of the calcium component is granulated together with these or other necessary components. At this time, the agent A and the agent B need to be granulated so as not to be classified. Usually, the calcium component is prepared as a chloride, and in the case of granules, the form of CaCl 2 .2H 2 O is stable. In addition, a small amount of additives such as acetic acid and glucose may be further added together with these as desired.

また、マグネシウム成分は、透析剤に用いられる濃度
ではB剤に配合することができるが、重曹と反応して難
溶性の固体を生成しやすいので、カルシウム成分ととも
にA剤に配合するのが好ましい。通常マグネシウム成分
は塩化物として調製され、造粒体の場合、MgCl2・6H2O
の形が安定している。
Further, the magnesium component can be blended with the agent B at the concentration used for the dialysis agent, but since it easily reacts with baking soda to form a hardly soluble solid, it is preferable to blend the magnesium component into the agent A together with the calcium component. Normally, the magnesium component is prepared as chloride, and in the case of granules, MgCl 2・ 6H 2 O
The shape is stable.

A剤およびB剤を造粒せしめる手段としては、各成分
を粉体のまま適宜水と共に混合し、適当な造粒機を用い
て造粒せしめることができる。次のような手段を採用す
ると、溶解性、特に重曹の溶解性を効果的に改善し得る
と共に、粒状体の取り扱いも容易であり、また強度も充
分であり、粉状化もし難く、均質で組成安定性の良い粒
状物が得られるので好ましい。A剤とB剤とを分級の起
こり難いように造粒するには特にこの方法が好ましい。
As a means for granulating the A agent and the B agent, each component can be appropriately mixed with water as powder and granulated using a suitable granulator. By adopting the following means, the solubility, particularly the solubility of sodium bicarbonate, can be effectively improved, the handling of the granular material is easy, the strength is sufficient, the powdering is difficult, and the uniformity is obtained. It is preferable because a granular material having good composition stability can be obtained. This method is particularly preferable for granulating the A agent and the B agent so that classification is unlikely to occur.

電解質成分粉末を粒度調製し、水分が0.5〜15重量%
となるように水を加えて充分混合し、押出し造粒機等に
より造粒後、乾燥することにより、顆粒状の製品とす
る。用いられる原料としての電解質成分粉末の粒子径と
しては250μ以下、好ましくは180μ以下、更に好ましく
は100μ以下を採用するのが適当である。粒子径が250μ
を超える場合には、最終品となる顆粒の機械的強度が不
十分となり、一部粉化したり、また溶解速度が遅くなる
ので好ましくない。また、造粒に際し水分が0.5重量%
に満たない場合には粒子強度が低く粉化し易くなり、逆
に15重量%を超える場合には造粒が困難となる恐れがあ
るので何れも好ましくない。かくして造粒される粒子の
粒径は0.1〜5mm程度にするのが適当である。粒状体の粒
径が前記範囲に満たない場合には流動性が阻害された
り、粉化して飛散したりして取扱いが困難となり、逆に
前記範囲を超える場合には粒子の機械的強度が低下した
り、溶解に時間がかかりすぎたりする恐れがあるので何
れも好ましくない。
The particle size of the electrolyte component powder is adjusted, and the water content is 0.5 to 15% by weight.
Water is added to the mixture, and the mixture is sufficiently mixed, granulated by an extrusion granulator or the like, and then dried to obtain a granular product. It is appropriate that the particle diameter of the electrolyte component powder as a raw material to be used is 250 μm or less, preferably 180 μm or less, more preferably 100 μm or less. Particle size 250μ
If the ratio exceeds the above range, the mechanical strength of the granules as the final product becomes insufficient, and the granules are partially powdered and the dissolution rate is undesirably reduced. In addition, moisture is 0.5% by weight during granulation.
If the amount is less than 15%, the particle strength is low and the powder is easily powdered. On the other hand, if the amount exceeds 15% by weight, granulation may be difficult, so neither is preferable. The particle size of the particles thus granulated is suitably about 0.1 to 5 mm. If the particle size of the granular material is less than the above range, the fluidity is impaired, or the powder is scattered and becomes difficult to handle, and if it exceeds the above range, the mechanical strength of the particles decreases. Or dissolution may take too long.

造粒物、特にB剤の乾燥に際しては、重曹の分解防止
や酢酸ガスの蒸散抑制の理由により、炭酸ガス雰囲気や
酢酸ガス雰囲気が用いるのが好ましい。炭酸ガスや酢酸
ガスの雰囲気を用いる場合には、炭酸ガス濃度としては
5%程度以上、酢酸ガス濃度としては0.05〜5%程度を
採用するのが適当である。
When drying the granulated material, particularly the agent B, it is preferable to use a carbon dioxide gas atmosphere or an acetic acid gas atmosphere for the purpose of preventing decomposition of sodium bicarbonate and suppressing evaporation of acetic acid gas. When using an atmosphere of carbon dioxide gas or acetic acid gas, it is appropriate to employ a carbon dioxide gas concentration of about 5% or more and an acetic acid gas concentration of about 0.05 to 5%.

乾燥は30〜90℃において行なうのが適当であり、具体
的乾燥手段としては例えば、バンド乾燥機、円板乾燥
機、通気乾燥機、回転乾燥機等を採用することにより、
高強度及び易溶性で均一で組成安定性の良好な顆粒を得
ることが可能となる。
Drying is suitably performed at 30 to 90 ° C., and specific drying means include, for example, a band dryer, a disk dryer, a through-air dryer, a rotary dryer, and the like.
It is possible to obtain granules having high strength, high solubility, uniformity and good composition stability.

かくして得られた粒状体は溶解速度(本粒状体9.3gを
25℃の水1000mlに溶解したとき、液が透明になる迄の所
要時間)は3分以内となり、粒状体の安息角(細川ミク
ロン(株)製のパウダーテスターで測定)は50度以下で
あり、溶解性及び流動性等の取り扱い上極めて良好なも
のが得られる。又、これら粒状体の包装は、密閉状態、
好ましくは炭酸ガスと共に封入することにより、分解、
変質をより一層防止することが可能となる。
The granular material thus obtained has a dissolution rate (9.3 g of this granular material
The time required for the solution to become transparent when dissolved in 1000 ml of water at 25 ° C is less than 3 minutes, and the angle of repose (measured with a powder tester manufactured by Hosokawa Micron Co., Ltd.) is 50 degrees or less. Very good in handling such as solubility, fluidity and the like can be obtained. In addition, the packaging of these granular materials is sealed,
Decomposition, preferably by encapsulation with carbon dioxide,
Deterioration can be further prevented.

かくして本発明による透析用剤を使用する際には、こ
れを常法に従い、水溶液として透析液に供する。本発明
による透析用剤と従来法による透析用剤とを比較する
と、従来においては重曹を約6重量%の濃厚液とし、こ
れを水を用いて27倍に希釈したもの34容に対し、他の電
解質成分溶液1容を混合し、透析液とするのに対し、本
透析用剤は、単に100倍の水で溶解するだけで透析液に
することが可能となる。
Thus, when the dialysis agent according to the present invention is used, it is supplied to the dialysate as an aqueous solution according to a conventional method. A comparison between the dialysis agent of the present invention and the dialysis agent according to the conventional method shows that, in the prior art, about 6% by weight of sodium bicarbonate was concentrated and diluted 27 times with water. Is mixed with 1 volume of the electrolyte component solution to obtain a dialysis solution. On the other hand, the present dialysis agent can be made into a dialysis solution simply by dissolving with 100 times water.

本発明の透析用剤においては、溶解したあとのpHを調
整する目的で予め酢酸のようなpH調整成分を含むもので
あってもよい。pH調整成分は溶解後の透析液に加えても
よい。
The dialysis agent of the present invention may contain a pH adjusting component such as acetic acid in advance for the purpose of adjusting the pH after dissolution. The pH adjusting component may be added to the dialysate after dissolution.

また、本発明のB剤において、重曹と共に粒状化し得
る成分としては、カルシウム成分を含まない電解質成分
の一種以上であるが、これらのうち大量に必要とされる
成分を重点的に重曹と共に粒状化するのが効果的であ
る。この場合、A剤については、カルシウムを含む電解
質成分が他の電解質成分に比し、必要量が比較的少ない
為、これらを別個に用意しても使用の際にさほど不便を
来さない。別個に用意する形態としては、粉体状でも溶
液状でも構わない。例えば、カルシウムを含む電解質成
分を水溶液(塩化物)として用意する場合には、一般に
貯留性や搬送の点から100〜200cc程度の容量を採用する
のが適当である。A剤が、水溶液の形態の場合でも、マ
グネシウム成分をA剤に配合することが好ましい。
In the agent B of the present invention, the component that can be granulated together with baking soda is at least one of an electrolyte component that does not contain a calcium component. Of these, components that are required in large amounts are mainly granulated together with baking soda. It is effective to do. In this case, since the required amount of the electrolyte component containing calcium is relatively smaller than that of the other electrolyte components, the preparation of the agent A does not cause much inconvenience when used separately. As a form prepared separately, a powder form or a solution form may be used. For example, when preparing an electrolyte component containing calcium as an aqueous solution (chloride), it is generally appropriate to adopt a capacity of about 100 to 200 cc from the viewpoint of storage properties and transport. Even when the agent A is in the form of an aqueous solution, it is preferable to mix the magnesium component with the agent A.

[実施例] 実施例1 それぞれ平均粒径50μ程度に粉砕された重炭酸ナトリ
ウム、塩化ナトリウム、塩化カリウム及び酢酸ナトリウ
ム3水和物を下記の比率で混合し、更に5重量%の水を
添加して混合した。
Example 1 Example 1 Sodium bicarbonate, sodium chloride, potassium chloride and sodium acetate trihydrate, each ground to an average particle size of about 50 μm, were mixed in the following ratio, and 5% by weight of water was further added. And mixed.

NaHCO3 27.072重量% NaCl 62.155 〃 KCl 1.995 〃 CH3COONa・3H2O 8.778 〃 該混合物を双軸型造粒機を用い平均粒径400μの粒子
を500kg得た。次いで、炭酸ガス濃度20%及び酢酸ガス
0.5%を含む温度50℃に調整された雰囲気下で、回分式
箱型乾燥機に前記粒子を入れ3時間乾燥せしめた。得ら
れた造粒物は顆粒状であり、平均粒子径は0.4mmであ
り、安息角は40度であり、良好な流動性を持っており、
25℃の水に溶解した時の溶解速度は1.5分であった。上
記製品から任意に5個のサンプル(9.3085g)を取り、2
5℃の水で全容積1000mlに溶解した。結果を第1表に示
す。
NaHCO 3 27.072% by weight NaCl 62.155 KCl 1.995 CH 3 COONa.3H 2 O 8.778 500 g of particles having an average particle diameter of 400 μm were obtained from the mixture using a twin-screw granulator. Then, carbon dioxide concentration 20% and acetic acid gas
In an atmosphere containing 0.5% and adjusted to a temperature of 50 ° C., the particles were placed in a batch box dryer and dried for 3 hours. The obtained granules are granular, the average particle size is 0.4 mm, the angle of repose is 40 degrees, and has good fluidity,
The dissolution rate when dissolved in water at 25 ° C. was 1.5 minutes. Take 5 samples (9.3085g) arbitrarily from the above product,
Dissolved in water at 5 ° C. to a total volume of 1000 ml. The results are shown in Table 1.

上記第1表より、この造粒物を無作為に採取したの
ち、カルシウム、マグネシウム成分を適宜加えることに
より5点の試料共極めて均一な組成を有する透析液に復
元できることが明らかである。
From Table 1 above, it is clear that after collecting the granules at random, the calcium and magnesium components can be appropriately added to restore the dialysate having a very uniform composition for all five samples.

次いで、この造粒物の長期保存による経時変化を調べ
た。得られた造粒物を密閉包装し室温下に放置して、製
造直後、1ケ月後、3ケ月後、6ケ月後及び12ケ月経過
後に、それぞれ所定量(9.3085g)を取り25℃の水で全
容積1000mlに溶解した。得られた溶解液について、その
pH及び製造直後の各イオン濃度を100としてこれに対す
る偏差を求めた結果を第2表に示す。
Next, the change over time due to long-term storage of the granulated product was examined. The obtained granules are hermetically packed and allowed to stand at room temperature. Immediately after production, 1 month, 3 months, 6 months and 12 months have elapsed, a predetermined amount (9.3085 g) was taken, and water at 25 ° C. To dissolve in a total volume of 1000 ml. About the obtained solution,
Table 2 shows the results obtained by assuming that the pH and each ion concentration immediately after the production were 100, and the deviation from this was determined.

第2表よりこの造粒物は経時的に極めて安定であり、
長期保存後も製造直後と実質的に変らぬ透析液に復元で
きることが明らかである。
According to Table 2, this granulated product is extremely stable over time.
It is clear that the dialysate can be restored to a substantially unchanged state immediately after production even after long-term storage.

比較例1 それぞれ平均粒径50μ程度に粉砕された塩化ナトリウ
ム、塩化カリウム、塩化カルシウム、塩化カルシウム2
水和物、塩化マグネシウム6水和物及び酢酸ナトリウム
3水和物を下記の比率で混合し、更に5重量%の水を添
加して混合した。
Comparative Example 1 Sodium chloride, potassium chloride, calcium chloride, calcium chloride each pulverized to an average particle size of about 50 μm
The hydrate, magnesium chloride hexahydrate and sodium acetate trihydrate were mixed in the following ratio, and 5% by weight of water was further added and mixed.

NaCl 80.389重量% KCl 2.580 〃 CaCl2・2H2O 3.573 〃 MgCl2・6H2O 2.104 〃 CH3COONa・3H2O 11.354 〃 該混合物を双軸型造粒機を用い平均粒径450μの粒子
を500kg得た。次いで酢酸ガス0.5%を含む温度50℃に調
整された雰囲気下で、回分式箱型乾燥機に前記粒子を入
れ3時間乾燥せしめた。得られた粒子(A剤と称す)は
顆粒状であり、平均粒子径は0.45mmであり、安息角は40
度であり、良好な流動性を示した。
NaCl 80.389 wt% KCl 2.580 〃 CaCl 2・ 2H 2 O 3.573 〃 MgCl 2・ 6H 2 O 2.104 〃 CH 3 COONa ・ 3H 2 O 11.354 500 kg was obtained. Next, the particles were placed in a batch box dryer under an atmosphere containing 0.5% acetic acid gas and adjusted to a temperature of 50 ° C., and dried for 3 hours. The obtained particles (referred to as “A agent”) are granular, have an average particle diameter of 0.45 mm, and have a repose angle of 40.
Degree and showed good fluidity.

他方、平均粒径50μ程度に粉砕された重曹に5重量%
の水を添加混合し、双軸型造粒機にて造粒し平均粒径45
0μの粒子を200kg得た。次いで、炭酸ガス濃度20%を含
む温度50℃に調整された雰囲気下で、回分式箱型乾燥機
に前記粒子を入れ3時間乾燥せしめた。得られた粒子
(B剤と称す)は顆粒状であり、平均粒子径は0.45mmで
あり良好な流動性を示した。
On the other hand, 5% by weight
Water was added and mixed, and the mixture was granulated with a twin-screw granulator to give an average particle size of 45.
200 kg of 0 micron particles were obtained. Next, the particles were placed in a batch-type box dryer under an atmosphere adjusted to a temperature of 50 ° C. containing a carbon dioxide gas concentration of 20%, and dried for 3 hours. The obtained particles (referred to as agent B) were granular and had an average particle diameter of 0.45 mm, indicating good fluidity.

次に、前記A剤とB剤を2.856:1(重量比)で混合し
て、混合粉末500kgを得た。得られたA剤とB剤の混合
物(透析用剤と称す)の安息角は40度であり、良好な流
動性を持っており、25℃の水に溶解した時の溶解速度は
1分であった。上記透析用剤から任意に5個のサンプル
(9.7171g)を取り、25℃の水で全容積1000mlに溶解し
た結果を第3表に示す。
Next, the A agent and the B agent were mixed at a ratio of 2.856: 1 (weight ratio) to obtain 500 kg of a mixed powder. The obtained mixture of agent A and agent B (referred to as dialysis agent) has an angle of repose of 40 degrees, has good fluidity, and has a dissolution rate of 1 minute when dissolved in water at 25 ° C. there were. Table 3 shows the results obtained by arbitrarily taking five samples (9.7171 g) from the above dialysis agent and dissolving them in water at 25 ° C. in a total volume of 1000 ml.

上記第3表より、この透析用剤を無作為に採取したの
ち溶解したときは、5点の試料共極めて均一な組成を有
する透析液に復元できることが明らかである。次いで、
本発明による透析用剤の長期保存による経時変化を調べ
た。得られた透析用剤を密閉包装し室温下に放置して、
製造直後、1ケ月後、3ケ月後、6ケ月後及び12ケ月経
過後に、それぞれ所定量(9.7171g)を取り25℃の水で
全容積1000mlに溶解した。得られた溶解液について、そ
のpH及び製造直後の各イオン濃度を100としてこれに対
する偏差を求めた結果を第4表に示す。
From Table 3 above, it is clear that when the dialysis agent is randomly collected and then dissolved, the five samples can be reconstituted into a dialysate having a very uniform composition. Then
The temporal change of the dialysis agent according to the present invention due to long-term storage was examined. The obtained dialysis agent is hermetically packed and left at room temperature,
Immediately after production, one month, three months, six months, and 12 months later, a predetermined amount (9.7171 g) was taken and dissolved in water at 25 ° C. in a total volume of 1,000 ml. Table 4 shows the results obtained by assuming that the pH of the obtained solution and the respective ion concentrations immediately after the production were 100, and the deviation from this was obtained.

第4表より、この透析用剤は経時的に極めて安定であ
り、長期保存後も製造直後と実質的に変らぬ透析液に復
元できることが明らかである。
From Table 4, it is clear that this dialysis agent is extremely stable over time and can be restored to a dialysate substantially unchanged from immediately after production even after long-term storage.

[発明の効果] 本発明の透析用剤は容易に水に溶解して均質な水溶液
になり簡単に透析液を得ることができる。また、本透析
用剤は、体積が小さくでき、貯留時に粉化したりあるい
は難溶性の化合物が生成したりせず保存あるいは輸送に
有利である。さらに、流動性に優れるので、取り扱いが
容易である。
[Effect of the Invention] The dialysis agent of the present invention can be easily dissolved in water to form a homogeneous aqueous solution, and a dialysate can be easily obtained. In addition, the present dialysis agent can be reduced in volume, and is advantageous for storage or transport without powdering during storage or formation of a hardly soluble compound. Furthermore, since it is excellent in fluidity, handling is easy.

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭56−131515(JP,A) 特開 平3−38527(JP,A) 特開 昭57−88116(JP,A) 米国特許4489535(US,A) 仲井由宣ら編「新製剤学」1987.4. 1 南山堂 115〜116頁 化学大辞典編集委員会編「化学大辞典 5」1987.2.15.共立出版 726頁 化学大辞典編集委員会編「化学大辞典 3」1987.2.15.共立出版 810頁 (58)調査した分野(Int.Cl.6,DB名) A61K 33/00 A61K 33/06 A61K 33/14 CA(ONLINE) WPIL(DERWENT)──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-56-131515 (JP, A) JP-A-3-38527 (JP, A) JP-A-57-88116 (JP, A) US Patent 4,489,535 (US , A) Yoshinobu Nakai et al., “New Pharmaceutical Sciences”, 1987.4.1, Nanzando, pp. 115-116, edited by the Chemical Dictionary Editor's Committee, “Chemical Dictionary 5”, 1987.2.15. Kyoritsu Shuppan, 726 pages, Dictionary of Chemistry Dictionary, edited by the Dictionary of Chemistry 3, 1987.2.15. Kyoritsu Shuppan 810 pages (58) Fields investigated (Int. Cl. 6 , DB name) A61K 33/00 A61K 33/06 A61K 33/14 CA (ONLINE) WPIL (DERWENT)

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】カルシウム成分を含み重曹を含まない群か
らなる造粒物(A剤)と、重曹を含みカルシウム成分を
含まない群からなる造粒物(B剤)との混合物であっ
て、B剤が塩化ナトリウム、塩化カリウム及び酢酸ナト
リウムから選ばれた少なくとも1種の電解質成分と重曹
とからなる均質な造粒物であり、かつ、A剤とB剤の粒
径は平均粒径が大きな剤の平均粒径に対する小さな剤の
平均粒径の比が0.9以上であることを特徴とする透析用
剤。
1. A mixture of a granulated product comprising a group containing a calcium component and not containing baking soda (agent A) and a granulated product containing a group containing baking soda and containing no calcium component (agent B), The agent B is a homogeneous granulated product comprising at least one electrolyte component selected from sodium chloride, potassium chloride and sodium acetate and baking soda, and the particle diameters of the agent A and the agent B are large. A dialysis agent, wherein the ratio of the average particle size of the small agent to the average particle size of the agent is 0.9 or more.
【請求項2】透析用剤の溶解速度が3分以内である請求
項1記載の透析用剤。
2. The dialysis agent according to claim 1, wherein the dissolution rate of the dialysis agent is within 3 minutes.
【請求項3】透析用剤の安息角が50度以下である請求項
1又は2記載の透析用剤。
3. The dialysis agent according to claim 1, wherein the angle of repose of the dialysis agent is 50 degrees or less.
【請求項4】塩化ナトリウム、塩化カリウム及び酢酸ナ
トリウムから選ばれた少なくとも1種の電解質成分粉末
と重曹粉末を、水分が0.5〜15重量%となるように水を
添加して混合し、造粒、乾燥して造粒物(B剤)を製造
し、カルシウム成分を含み重曹を含まない群からなる造
粒物(A剤)と混合することを特徴とする請求項1〜3
のいずれか1項に記載の透析用剤の製造方法。
4. Granulation of at least one electrolyte component powder selected from sodium chloride, potassium chloride and sodium acetate and sodium bicarbonate powder by adding water to a water content of 0.5 to 15% by weight. 4. A granulated product (agent B) is produced by drying and mixed with a granulated material (agent A) comprising a group containing a calcium component and not containing sodium bicarbonate.
The method for producing a dialysis agent according to any one of the above.
【請求項5】前記の乾燥を、炭酸ガス雰囲気中で行うこ
とを特徴とする請求項4記載の透析用剤の製造方法。
5. The method for producing a dialysis agent according to claim 4, wherein said drying is performed in a carbon dioxide gas atmosphere.
JP1206940A 1989-08-11 1989-08-11 Dialysis agent and method for producing the same Expired - Fee Related JP2986810B2 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP1206940A JP2986810B2 (en) 1989-08-11 1989-08-11 Dialysis agent and method for producing the same
US07/564,159 US5071558A (en) 1989-08-11 1990-08-08 Sodium bicarbonate dialysate
DE69018172T DE69018172T3 (en) 1989-08-11 1990-08-09 Composition containing sodium bicarbonate for the preparation of a dialysis solution.
EP90115320A EP0417478B2 (en) 1989-08-11 1990-08-09 Sodium bicarbonate containing mixture for producing a dialysis solution
CA002023075A CA2023075C (en) 1989-08-11 1990-08-10 Sodium bicarbonate dialysate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1206940A JP2986810B2 (en) 1989-08-11 1989-08-11 Dialysis agent and method for producing the same

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JPH0374331A JPH0374331A (en) 1991-03-28
JP2986810B2 true JP2986810B2 (en) 1999-12-06

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Country Link
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2986256B2 (en) * 1991-09-12 1999-12-06 扶桑薬品工業株式会社 Granules for hemodialysis
JP3415291B2 (en) * 1994-09-27 2003-06-09 味の素ファルマ株式会社 Bicarbonate dialysis agent
JP2005194199A (en) * 2003-12-26 2005-07-21 Shimizu Pharmaceutical Co Ltd Solid dialysis agent and method for producing the same
JP2005239618A (en) * 2004-02-26 2005-09-08 Ajinomoto Co Inc Method for producing powdery dialysis preparation
JP2007037601A (en) * 2005-07-29 2007-02-15 Ajinomoto Co Inc Solid agent a for dialysis which has improved solubility

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4489535A (en) 1980-10-02 1984-12-25 Veltman Preston Leonard Materials and method for preparing dialysis solutions containing bicarbonate ions

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4489535A (en) 1980-10-02 1984-12-25 Veltman Preston Leonard Materials and method for preparing dialysis solutions containing bicarbonate ions

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
仲井由宣ら編「新製剤学」1987.4.1 南山堂 115〜116頁
化学大辞典編集委員会編「化学大辞典3」1987.2.15.共立出版 810頁
化学大辞典編集委員会編「化学大辞典5」1987.2.15.共立出版 726頁

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