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JPH04112830A - Preparation of liquid composition for cleaning enteric canal - Google Patents

Preparation of liquid composition for cleaning enteric canal

Info

Publication number
JPH04112830A
JPH04112830A JP23123790A JP23123790A JPH04112830A JP H04112830 A JPH04112830 A JP H04112830A JP 23123790 A JP23123790 A JP 23123790A JP 23123790 A JP23123790 A JP 23123790A JP H04112830 A JPH04112830 A JP H04112830A
Authority
JP
Japan
Prior art keywords
electrolyte
polyethylene glycol
granules
composition
spraying
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
JP23123790A
Other languages
Japanese (ja)
Inventor
Satoru Taguchi
哲 田口
Mitsusachi Ichiyama
市山 三幸
Yuji Kodama
児玉 裕治
Yasuhiro Hatsuda
泰弘 初田
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.)
Morishita Pharmaceuticals Co Ltd
Original Assignee
Morishita Pharmaceuticals 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 Morishita Pharmaceuticals Co Ltd filed Critical Morishita Pharmaceuticals Co Ltd
Priority to JP23123790A priority Critical patent/JPH04112830A/en
Publication of JPH04112830A publication Critical patent/JPH04112830A/en
Pending legal-status Critical Current

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  • Medicinal Preparation (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)

Abstract

PURPOSE:To produce the subject composition in the form of granules having excellent flowability and quickly soluble in water in use by uniformly mixing an electrolyte in molten polyethylene glycol and spraying the mixture. CONSTITUTION:Granules having an average particle diameter of 250-300mum are produced by charging a polyethylene glycol in a melting tank, melting by heating at 60-100 deg.C, adding 10-20% electrolyte (e.g. Na or K salt of an organic acid, NaCl, KCl, Na2SO4 and NaHCO3) having a particle diameter of >=50mum to the molten liquid, dispersing the electrolyte with a stirrer, supplying the dispersed liquid to a sprayer and spraying into a chamber of -30 to +30 deg.C. Since the granule has spherical form, it has excellent flowability and is easily handleable owing to its low stickiness. Accordingly, the production process can be easily automated to decrease the variation in filled amount in packaging and enable remarkable reduction of production cost.

Description

【発明の詳細な説明】 (1)産業上の利用分野 本発明は、腸管洗浄液用組成物の製造法に関する。[Detailed description of the invention] (1) Industrial application fields The present invention relates to a method for producing a composition for intestinal cleansing liquid.

(2)従来の技術 腸管の洗浄は、大腸内視鏡検査や二重造影バリウム注腸
検査において重要な前処置である。洗浄液としては電解
質組成液(BES:Ba1anced  EleCtr
Olyte  5oluti。
(2) Conventional Technique Cleaning of the intestinal tract is an important pretreatment for colonoscopy and double-contrast barium enema examination. As a cleaning solution, an electrolyte composition solution (BES: Ba1anced EleCtr
Olyte 5oluti.

n)、特殊組成電解質液(商品名、ゴライトリー(Go
lytely))及び特殊組成電解質液の改良液(WO
8710O754)が提案されている。また、従来の腸
管洗浄液用組成物は服用しずらく9体内の電解質バラン
スに悪影響を及ぼすことが予想されるなどいくつかの欠
点を有していたが、これらの欠点を克服する腸管洗浄液
が特開平2−25424号に開示されている。
n), special composition electrolyte solution (product name, Golightly)
lytely) and improved solution of special composition electrolyte solution (WO
8710O754) has been proposed. In addition, conventional intestinal cleansing liquid compositions had several drawbacks, such as being difficult to take and expected to have a negative effect on the electrolyte balance in the body, but a special intestinal cleansing liquid that overcomes these drawbacks has been developed. It is disclosed in JP-A No. 2-25424.

腸管洗浄液の製造については既に洗浄液成分を至適な粒
度に粉砕して混合する方法が特開平1135319号に
開示されている。
Regarding the production of intestinal cleansing liquid, Japanese Patent Application Laid-Open No. 1135319 has already disclosed a method in which cleansing liquid components are pulverized to an optimum particle size and mixed.

しかし、前述の製造法は製造工程数が多いうえ組成物の
流動性は悪い。そこで、各成分を粉砕し混合する方法に
代わる腸管洗浄液用組成物の製造法の開発が望まれてい
る。
However, the above-mentioned manufacturing method requires a large number of manufacturing steps and the fluidity of the composition is poor. Therefore, it is desired to develop a method for producing a composition for intestinal cleansing solution, which is an alternative to the method of grinding and mixing each component.

(3)発明が解決しようとする課題 各種の腸管洗浄液用組成物の中で、ポリエチレングリコ
ールと電解質を含む組成物を製造するに当たり、ポリエ
チレングリコールと電解質を均質化する工程が必要であ
る。この際、ポリエチレングリコールが組成中の約85
%を占め、他の組成物に比べ極端に含有量が高いこと、
またポリエチレングリコールと電解質の比重差が大きく
、均一に混合することが難しい。
(3) Problems to be Solved by the Invention In producing a composition containing polyethylene glycol and an electrolyte among various intestinal cleansing liquid compositions, a step of homogenizing the polyethylene glycol and the electrolyte is necessary. At this time, polyethylene glycol is about 85% of the composition.
%, and the content is extremely high compared to other compositions,
Furthermore, the difference in specific gravity between polyethylene glycol and electrolyte is large, making it difficult to mix them uniformly.

一般にこの様な場合の解決策として、滑沢側等の添加が
有効であるが、腸管洗浄という目的を考えると水に溶解
しない成分を添加することは好ましくない。また、既に
特開平1−135319号に開示されている粉砕によっ
て各成分の粒子径を調整する方法では粉砕、篩分けの工
程を目的の粒子径が得られるまで繰り返さなければなら
ず、これがコストアップの原因となっている。
Generally, as a solution to such cases, adding a lubricant or the like is effective, but considering the purpose of intestinal cleansing, it is not preferable to add components that are not soluble in water. Furthermore, in the method of adjusting the particle size of each component by crushing, which has already been disclosed in JP-A-1-135319, the process of crushing and sieving must be repeated until the desired particle size is obtained, which increases costs. It is the cause of

さらに、ポリエチレングリコールの粉砕はポリエチレン
グリコールの凝固点が低いために、通常用いられる粉砕
機で粉砕すると溶融してしまう。
Furthermore, since polyethylene glycol has a low freezing point, it will melt if it is crushed with a commonly used crusher.

そこで、粉砕装置内を冷却するなど特殊な条件設定が必
要である。しかもポリエチレングリコールの粉砕物は粒
子径が不定形で、付着性があるため流動性が悪く、分包
工程で充填バラツキを生し易い。
Therefore, it is necessary to set special conditions such as cooling the inside of the crushing device. Moreover, the pulverized polyethylene glycol has an irregular particle size and has poor fluidity due to its adhesive properties, and tends to cause filling variations in the packaging process.

組成物の流動性と同様に問題になるのがポリエチレング
リコールの溶解性である。各成分の均一性を高めるため
に非常に細かいポリエチレングリコールを用いた場合は
溶解時に凝集し薬液調製時間が長くなる。従って、本発
明は流動性、溶解性及び均一性に優れた腸管洗浄液用組
成物を製造することを目的とする。
Similar to the fluidity of the composition, the solubility of polyethylene glycol is a problem. If very fine polyethylene glycol is used to improve the uniformity of each component, it will aggregate during dissolution, prolonging the preparation time of the drug solution. Therefore, an object of the present invention is to produce a composition for intestinal cleansing liquid having excellent fluidity, solubility, and uniformity.

(4)課題を解決するための手段 本発明者らは、上記の問題点を克服するために種々検討
を行った結果、ポリエチレングリコールの凝固点が低い
ことを利用して、ポリエチレングリコールを溶融させた
状態で電解質を均一に混合し噴霧すると、各成分が均一
に混合された球形の造粒物が得られることを見いだした
。また、この造粒物の流動性及び溶解性を調べた結果、
特開平1−135319号に開示されている各成分の粉
砕品を混合する方法に比べ優れていることが判明した。
(4) Means for Solving the Problems The present inventors conducted various studies to overcome the above problems, and as a result, they melted polyethylene glycol by taking advantage of its low freezing point. It has been found that if the electrolyte is uniformly mixed and sprayed under the condition, spherical granules in which each component is uniformly mixed can be obtained. In addition, as a result of examining the fluidity and solubility of this granule,
It has been found that this method is superior to the method disclosed in JP-A-1-135319, in which pulverized products of each component are mixed.

それらの知見に基づいて初期の目的を達成する本願発明
を完成することができた。
Based on these findings, we were able to complete the present invention which achieves the initial objective.

すなわち、本発明はポリエチレングリコールを溶融させ
た状態で電解質を均一に混合し噴霧することを特徴とす
る腸管洗浄液用組成物の製造法である。
That is, the present invention is a method for producing a composition for intestinal cleansing liquid, which is characterized by uniformly mixing and spraying an electrolyte in a state in which polyethylene glycol is melted.

本発明の製造法は、例えばポリエチレングリコールと電
解質が相対的に下記の範囲に含まれる腸管洗浄液用組成
物の製造に利用でき、好ましい実施態様を示せば次の通
りである。
The production method of the present invention can be used, for example, to produce a composition for intestinal cleansing liquid in which polyethylene glycol and electrolyte are contained in the following relative ranges, and preferred embodiments are as follows.

ポリエチレングリコール  10〜150gに対し 有機酸のナトリウム塩     O〜60mmol有機
酸のカリウム塩      0〜121111101塩
化ナトリウム        7〜60m1Ilol塩
化カリウム          O〜12IIIlol
硫酸ナトリウム         O〜44mmol炭
酸水素ナトリウム      O〜23++mol(但
し、カリウムイオンとして2〜12’mEq)まず、ポ
リエチレングリコールの処方量を秤取して溶解タンクに
投入し、このタンクを60°C〜100℃付近まで加温
する。常温で固体のポリエチレングリコールの凝固点は
53℃〜57℃であるため、ポリエチレングリコールは
溶融して液体となる。この溶液に各電解質をそれぞれ処
方量秤取して添加し、撹拌機を用いて分散させる。通常
、分散液中の電解質の粒度は、100μm以下で、好ま
しくは50μm以下である。また、電解質の比率は、通
常10〜50%の範囲が適当であるが、好ましくは10
〜20%である。 分散終了後、定量ポンプを用いて噴
霧装置に分散液を供給する。
For 10-150 g of polyethylene glycol Sodium salt of organic acid O-60 mmol Potassium salt of organic acid 0-121111101 Sodium chloride 7-60 ml Ilol Potassium chloride O-12 IIIlol
Sodium sulfate O ~ 44 mmol Sodium hydrogen carbonate O ~ 23++ mol (however, 2 ~ 12'mEq as potassium ion) First, the prescribed amount of polyethylene glycol is weighed and put into a dissolution tank, and this tank is heated at 60°C to 100°C. Warm up to the vicinity. Since polyethylene glycol, which is solid at room temperature, has a freezing point of 53°C to 57°C, polyethylene glycol melts and becomes liquid. A prescribed amount of each electrolyte is added to this solution by weighing, and dispersed using a stirrer. Typically, the particle size of the electrolyte in the dispersion is less than 100 μm, preferably less than 50 μm. In addition, the ratio of electrolyte is usually appropriate in the range of 10 to 50%, but preferably 10%.
~20%. After dispersion is completed, the dispersion liquid is supplied to the spray device using a metering pump.

この噴霧装置には回転ディスク式とスプレー式の2種類
があるがどちらを使用してもよい。室内の温度は分散液
が固形化する温度であれば何れでもよいが、通常−30
°C〜30°Cの範囲が好ましい。
There are two types of spraying devices: a rotating disk type and a spray type, and either of these can be used. The room temperature may be any temperature at which the dispersion solidifies, but it is usually -30°C.
A range of 0.degree. C. to 30.degree. C. is preferred.

また、室内を窒素等の不活性ガスで置換してもよく、ど
ちらでも対応できる噴霧冷却造粒装置が望ましい。噴霧
された分散液は、表面張力により球形となって落下し冷
却されて各成分が均一に混合された球形の造粒物を得る
ことができる。
Further, the interior of the room may be replaced with an inert gas such as nitrogen, and a spray cooling granulation device that can handle either of these is desirable. The sprayed dispersion becomes spherical and falls due to surface tension, and is cooled to obtain spherical granules in which each component is uniformly mixed.

この噴霧冷却造粒における造粒物の粒子径は、500 
am以上が5%以下で、75〜500μmが95%以上
、75μm以下が5%以下に調製することが好ましい。
The particle size of the granules in this spray cooling granulation is 500
It is preferable to adjust the thickness to 5% or less for am or more, 95% or more for 75 to 500 μm, and 5% or less for 75 μm or less.

また、造粒物の平均粒子径は通常100〜300μmで
、流動性、付着性及び溶解性を考慮すると好ましくは2
50〜300μmである。
In addition, the average particle diameter of the granules is usually 100 to 300 μm, and preferably 2 μm in consideration of fluidity, adhesion, and solubility.
It is 50 to 300 μm.

上記のごとく得られた組成物を常法に従って一回使用量
を分包し、臨床に供することができる。
The composition obtained as described above can be packaged in single-use doses according to a conventional method and used clinically.

分包に適用することのできる容器もしくは袋は水分透過
性及びガス透過性が無いものであれば、何れも使用でき
る。容器としては、ガラス容器、合成樹脂容器、金属容
器等が使用でき、袋としては、例えば、アルミニウムと
ラミネートした多層フィルム製のものが好適に使用でき
る。
Any container or bag that can be used for sachets may be used as long as it is not permeable to water or gas. As the container, a glass container, a synthetic resin container, a metal container, etc. can be used, and as the bag, for example, a bag made of a multilayer film laminated with aluminum can be suitably used.

(5)作用 本発明により調製した造粒物は球形であることから流動
性が良く付着性が少ないため製造工程におけるハンドリ
ングが優れている。その結果、製造工程の自動化が容易
となり、また分包工程における充填バラツキが減少する
(5) Effect Since the granulated material prepared according to the present invention is spherical, it has good fluidity and little adhesion, so it is easy to handle in the manufacturing process. As a result, the manufacturing process can be easily automated, and filling variations in the packaging process can be reduced.

また驚くべきことに本発明の方法により得られた造粒物
は粒度分布がロフト間変動により変化しても速やかに溶
解する特徴を持つことから、製品の粒度を厳しく管理す
る必要がなく篩下工程を簡略化できる。
Surprisingly, the granules obtained by the method of the present invention have the characteristic of quickly dissolving even if the particle size distribution changes due to fluctuations between lofts, so there is no need to strictly control the particle size of the product The process can be simplified.

(6)実施例 実施例1 予め、硫酸ナトリウム2.9kg、塩化ナトリウム0.
75kg、塩化カリウム0.38kg。
(6) Examples Example 1 2.9 kg of sodium sulfate and 0.0 kg of sodium chloride were prepared in advance.
75 kg, potassium chloride 0.38 kg.

炭酸水素ナトリウム0.8kgをそれぞれ秤取して、ロ
ッキングミキサー(愛知電機株式会社製)にて混合した
。この混合物をハンマータイプの粉砕機パルペライザ−
(細川ミクロン株式会社製ニスクリーン径0.5mm)
を用いて室温下にて粉砕した。この時、粉砕物の粒度分
布は20μm〜74ρmで平均粒子径は約40μmであ
った。次に、ポリエチレングリコール4000を30k
g秤取し、溶解用タンクに投入後、約80゛cに加温し
てポリエチレングリコール4000を溶融させ、この中
に、粉砕した電解質混合物を添加し、撹拌機を用いて分
散させた。この分散液をポンプを用いて噴霧冷却造粒装
置(大川原化工機株式会社製)に供給し噴霧冷却造粒を
行なった結果、造粒物27kgを得た。噴霧装置は回転
ディスク式を使用し、回転数は4000rpmで、室内
の温度は約5°Cであった。
0.8 kg of sodium hydrogen carbonate was weighed out and mixed using a rocking mixer (manufactured by Aichi Denki Co., Ltd.). This mixture is passed through a hammer type pulverizer.
(Niclean diameter 0.5mm manufactured by Hosokawa Micron Co., Ltd.)
The mixture was pulverized at room temperature. At this time, the particle size distribution of the pulverized product was 20 μm to 74 μm, and the average particle diameter was about 40 μm. Next, add 30k of polyethylene glycol 4000.
After weighing and putting it into a dissolution tank, it was heated to about 80°C to melt polyethylene glycol 4000, and the pulverized electrolyte mixture was added thereto and dispersed using a stirrer. This dispersion liquid was supplied to a spray cooling granulation device (manufactured by Okawara Kakoki Co., Ltd.) using a pump and spray cooling granulation was performed, resulting in 27 kg of granules. A rotating disk type spraying device was used, the rotation speed was 4000 rpm, and the room temperature was about 5°C.

この造粒物をパウダーテスター(細川ミクロン株式会社
製)及びシーブシェイ力−(飯田製作所型)で測定し、
次の結果を得た。
The granules were measured with a powder tester (manufactured by Hosokawa Micron Co., Ltd.) and a sieve shear force (Iida Seisakusho type),
I got the following results.

平均粒子径 250μm 粒度分布  500μm以上   1.2%75〜50
0μm98.7% 75μm以下    0.1% 次に、この造粒物を自動分包機(名古屋東陽機械製作所
製)を用いて、ラミネート(ポリエステル、ポリエチレ
ン、アルミニウムの多層ラミネート)袋に137gずつ
充填することによって腸管洗浄液2f用分包品を得た。
Average particle diameter 250μm Particle size distribution 500μm or more 1.2%75-50
0μm98.7% 75μm or less 0.1% Next, each 137g of this granulated material is filled into a laminate (multilayer laminate of polyester, polyethylene, and aluminum) bag using an automatic packaging machine (manufactured by Nagoya Toyo Kikai Seisakusho). A packaged product for intestinal cleansing liquid 2f was obtained.

なお、1包の充填量は必要に応じて変えることができ、
例えば1!用として68.7g、32用として206g
、41用として275gとしてもよい。
In addition, the filling amount of one package can be changed as necessary.
For example 1! 68.7g for 32, 206g for 32
, 275g for 41.

実施例2 予め、塩化ナトリウム0.47kg、塩化カリウムQ、
30kg、クエン酸ナトリウム4.11kgをそれぞれ
秤取して、ロッキングミキサー(愛知電機株式会社製)
にて混合した。この混合物をハンマータイプの粉砕機パ
ルペライザ−(細川ミクロン株式会社製ニスクリーン径
0. 5mm)を用いて室温下にて粉砕した。
Example 2 In advance, 0.47 kg of sodium chloride, potassium chloride Q,
Weigh out 30 kg and 4.11 kg of sodium citrate, and place them in a rocking mixer (manufactured by Aichi Denki Co., Ltd.).
Mixed at . This mixture was pulverized at room temperature using a hammer type pulverizer (Niclean, diameter 0.5 mm, manufactured by Hosokawa Micron Co., Ltd.).

次に、ポリエチレングリコール4000を29゜95k
g秤取し、以下実施例1と同様な方法で造粒物27kg
を得た。
Next, add polyethylene glycol 4000 to 29°95k.
Weighed out 27 kg of granulated material in the same manner as in Example 1.
I got it.

比較例 比較試験に°用いるため表1に示した成分の腸管洗浄液
用組成物を特開平1−135319号に開示されている
方法により調製した。
Comparative Example A composition for intestinal cleansing liquid having the components shown in Table 1 was prepared for use in a comparative test by the method disclosed in JP-A-1-135319.

(余白) 表1 組成(g) 表2 含量測定結果 (7)試験例 試験例1 実施例1で製造した造粒物68.6g (lffiの洗
浄液を調製できる量)を5回秤取しそれぞれ含量試験を
行った。(表2) (余白) 試験の結果、実施例1で調製した造粒物中の各成分が均
一に分散している結果を得た。
(Margin) Table 1 Composition (g) Table 2 Content measurement results (7) Test example Test example 1 68.6 g of the granulated material produced in Example 1 (an amount that can prepare the cleaning solution for lffi) was weighed 5 times, and each A content test was conducted. (Table 2) (Margin) The test results showed that each component in the granules prepared in Example 1 was uniformly dispersed.

試験例2 実施例1で製造した造粒物と参考例で調製した組成物の
安定性試験を行ったところ、25°C及び40°C相対
湿度75%の保存条件に各6ケ月においたところ双方と
も含量、外観等の品質変化は認められず安定であった。
Test Example 2 A stability test was conducted on the granules produced in Example 1 and the composition prepared in Reference Example, and they were stored at 25°C and 40°C with a relative humidity of 75% for 6 months each. Both were stable with no changes in quality such as content or appearance.

試験例3 実施例1で得た分包品と、参考例で調製した組成物の分
包品の重量バラツキを比較した。(表裏3 分包品の充
填バラツキ 表4 溶解時間 試験の結果、本発明で調製した造粒物は特開平1−13
5319号に開示されている組成物に比べ充填バラツキ
が小さく流動性が優れている。
Test Example 3 The weight variations of the packaged product obtained in Example 1 and the packaged product of the composition prepared in Reference Example were compared. (Front and back 3 Filling variation of sachets Table 4 As a result of the dissolution time test, the granules prepared according to the present invention were
Compared to the composition disclosed in No. 5319, the filling variation is small and the fluidity is excellent.

試験例4 実施例1の造粒品と比較例の組成物について137g(
ただし、平均粒子径を300μm、200μm、150
μm及び100μmに調製)をそれぞれ攪拌下22の水
に完全に溶解するまでの時間を調べた。
Test Example 4 137g (137g) of the granulated product of Example 1 and the composition of Comparative Example
However, the average particle diameter is 300 μm, 200 μm, 150 μm.
The time required for complete dissolution of 22 μm and 100 μm of water under stirring was investigated.

試験の結果、表4に示すように、本発明の造粒品は平均
粒子径150μm、および100μmの溶解性が優れて
いる。
As shown in Table 4, the test results show that the granulated product of the present invention has an average particle size of 150 μm and excellent solubility of 100 μm.

(7)発明の効果 本発明の方法により、腸管洗浄液用組成物の各成分が均
一に混合され、また流動性に優れた造粒物を製造できる
ことから、製造工程の簡略化、自動化が計れ大幅なコス
トダウンが可能となる。さらに、使用に際し水溶液とし
て速やかに調製でき、その便益は大である。
(7) Effects of the invention By the method of the invention, each component of the composition for intestinal cleansing solution can be mixed uniformly, and a granulated product with excellent fluidity can be produced, which greatly simplifies and automates the manufacturing process. It is possible to reduce costs. Furthermore, it can be quickly prepared as an aqueous solution for use, which has great benefits.

Claims (1)

【特許請求の範囲】[Claims] (1)ポリエチレングリコールを溶融させた状態で電解
質を均一に混合し噴霧することを特徴とする腸管洗浄液
用組成物の製造法。
(1) A method for producing a composition for intestinal cleansing liquid, which comprises uniformly mixing and spraying an electrolyte in a molten state of polyethylene glycol.
JP23123790A 1990-08-31 1990-08-31 Preparation of liquid composition for cleaning enteric canal Pending JPH04112830A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23123790A JPH04112830A (en) 1990-08-31 1990-08-31 Preparation of liquid composition for cleaning enteric canal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23123790A JPH04112830A (en) 1990-08-31 1990-08-31 Preparation of liquid composition for cleaning enteric canal

Publications (1)

Publication Number Publication Date
JPH04112830A true JPH04112830A (en) 1992-04-14

Family

ID=16920471

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23123790A Pending JPH04112830A (en) 1990-08-31 1990-08-31 Preparation of liquid composition for cleaning enteric canal

Country Status (1)

Country Link
JP (1) JPH04112830A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003073260A (en) * 2001-08-30 2003-03-12 Nihon Pharmaceutical Co Ltd Composition for oral enterolavage liquid and packed preparation for the oral enterolavage liquid
US8999313B2 (en) 2012-09-11 2015-04-07 Norgine Bv Compositions
US9592252B2 (en) 2011-03-11 2017-03-14 Norgine Bv Colonoscopy—preparation

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003073260A (en) * 2001-08-30 2003-03-12 Nihon Pharmaceutical Co Ltd Composition for oral enterolavage liquid and packed preparation for the oral enterolavage liquid
US9592252B2 (en) 2011-03-11 2017-03-14 Norgine Bv Colonoscopy—preparation
US10646512B2 (en) 2011-03-11 2020-05-12 Norgine Bv Colonoscopy - preparation
US10780112B2 (en) 2011-03-11 2020-09-22 Norgine Bv Colonoscopy-preparation
US10792306B2 (en) 2011-03-11 2020-10-06 Norgine Bv Colonoscopy—preparation
US11529368B2 (en) 2011-03-11 2022-12-20 Norgine Bv Colonoscopy—preparation
US8999313B2 (en) 2012-09-11 2015-04-07 Norgine Bv Compositions
US9326969B2 (en) 2012-09-11 2016-05-03 Norgine Bv Compositions
US9707297B2 (en) 2012-09-11 2017-07-18 Norgine Bv Compositions
US10016504B2 (en) 2012-09-11 2018-07-10 Norgine Bv Compositions
US10918723B2 (en) 2012-09-11 2021-02-16 Norgine Bv Colon cleansing compositions and methods of use
US12083179B2 (en) 2012-09-11 2024-09-10 Norgine Bv Colon cleansing compositions and method of use

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