WO1997023232A1 - Verfahren zur schonenden keimreduzierung von pharmazeutischen zubereitungen - Google Patents
Verfahren zur schonenden keimreduzierung von pharmazeutischen zubereitungen Download PDFInfo
- Publication number
- WO1997023232A1 WO1997023232A1 PCT/EP1996/005578 EP9605578W WO9723232A1 WO 1997023232 A1 WO1997023232 A1 WO 1997023232A1 EP 9605578 W EP9605578 W EP 9605578W WO 9723232 A1 WO9723232 A1 WO 9723232A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- weight
- drug
- sterilized
- particularly preferably
- mbar
- Prior art date
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B5/00—Drying solid materials or objects by processes not involving the application of heat
- F26B5/04—Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K36/00—Medicinal preparations of undetermined constitution containing material from algae, lichens, fungi or plants, or derivatives thereof, e.g. traditional herbal medicines
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B9/00—Essential oils; Perfumes
- C11B9/02—Recovery or refining of essential oils from raw materials
- C11B9/025—Recovery by solvent extraction
Definitions
- compositions such as, for example, cut or powdered drugs and foods, e.g. Cut or ground spice drugs must not be sterilized in Germany or in other countries using methods which are highly effective and which correspond to the best state of the art.
- germ-reducing methods e.g. of the cobalt 60 or linear accelerators
- these radiation methods for reducing germs in herbal drugs or foods are among the most effective methods, there are national prohibitions by the legislation to use such methods due to strong concerns. This problem is related to the risk of the formation of toxic substances.
- a particularly serious disadvantage of hydrothermal processes is the fact that they operate at high temperatures, e.g. B. a Satt ⁇ steam temperature between 1 1 0 and 1 60 ° C. From this it can be seen that, in particular, drugs containing essential oils are sterilized, but unfortunately they lose their initial characteristics. In addition to the physical reduction of substances in the starting material, there are chemical changes that irreversibly convert or break down other ingredients of the drug material. Both the high temperatures in these hydrothermal sterilization processes and the radiation generate oxygen radicals, which irreversibly changes the flavonoid and polyphenol content of the drug material. In the case of fumigation with ethylene oxide, carcinogenic intermediate stages of the plant constituents arise, which must be avoided in any case.
- DAB 10 prescribes the following maximum bacterial values: for aerobes 10 5 , for fungi and yeasts 10 3 , for enterobacteria 10 3 , for E. coli 10 ⁇ , whereby no salmonella may be contained.
- the DAB 10 has higher maximum permissible numbers of bacteria.
- the maximum values for aerobes are 10 7 , for mushrooms and yeasts 10 4 , for enterobacteria 10 4 , for E. coli 10 2 and for Salmonella 0 per g of material.
- Very similar values apply to the European Pharmacopoeia, which was valid nationally from 1.1.1996, whereby this even allows a maximum of 10 4 fungi for herbal medicinal preparations for internal administration, although no E. coli or salmonella germs may be present.
- the maximum germ count recommendations of the German committee for medicinal, aromatic and aromatic plants of the producers of medicinal and aromatic plants are based on the regulations of DAB 10, so that the same maximum bacterial count values must be observed.
- the Swiss Pharmacopoeia (Pharmacopöa Helvetica VII) allows a maximum germ content of yeast at 10 4 / g, whereby only perceptible mold is not permitted with regard to mold, with E. Coli at most 10 2 / g and Salmonella should not be detectable.
- the object of the invention is therefore to provide a method that greatly reduces the number of germs while maintaining the Structure and qualitative and quantitative effects as well as the amount of ingredients.
- Such a drying system is known under the name INOX-MAURER vacuum dryer.
- Corresponding systems are also known under the name Riniker-MZA multi-purpose system or INOX-GLATT (Maurer) vacuum dryer.
- These vacuum drying systems are characterized by the fact that they have a multi-leg agitator with their own drive, which extends through a cylindrical mixing and drying chamber, these systems, if necessary, each with a filter, a backwashing device, a solvent condenser with aftercooler and collecting vessel, and recondensation gate and / or a process, control and regulation unit are provided.
- IUT-INOX universal dryers e.g. B. called the type l UT 20 or l UT 50.
- the pressure ratios when carrying out the sterilization process according to the invention are set so that when the water / ethanol mixture used for the sterilization is evaporated, a pressure of 1 to 600 mbar, preferably 1 0 to 200 mbar and in a particularly preferred manner 50 to 150 mbar is set .
- the suitable concentrations of ethanol in the hydroalcoholic mixture are between 10 and 96%, preferably from 30 to 90% or 40 to 80%. Another preferred range is 20 to 75%, with a 70% concentration being very particularly preferred.
- the quantitative ratio of the drug to be sterilized, possibly powdered, to the ethanol / water mixture is 1 00:50 to 50: 1 00.
- the temperatures to be selected for drying are between 25 ° C. and 90 ° C. for the heating jacket, the range from 65 ° C. to 75 ° C. being preferred.
- the product temperature is adjusted so that it is 10 to 60 ° C, preferably 20 to 40 ° C and most preferably 25 to 35 ° C.
- the disinfection is carried out in such a way that cut or milled drugs, if necessary for further processing into pharmaceutical preparations, are mixed with a mixture of ethanol and water, a mixture of 80% ethanol and the rest water or 70% ethanol and the rest of water is particularly preferred, and after exposure for several days, for example from 2 to 15 days, is then gently treated with the drying system described above while observing the parameters described above.
- the particularly preferred quantitative ratios of drug to the ethanol / water mixture are 100:90 to 10:90, in particular 50:50.
- the agitator is switched on depending on the need and consistency of the material to be sterilized.
- the following table lists a number of comparative values on the basis of frequently used plant drugs.
- a comparative disinfection was carried out on the basis of a drying process, the drying of the drug to be treated or the removal of the alcohol / water mixture for comparison was carried out under the normal pressure conditions according to the prior art.
- the product temperature during the drying according to the prior art, just as in the sterilization according to the invention, was between 25 and 35 ° C .; this was done in a conventional drying chamber.
- Example 1 Flos Sambuci
- Example 2 Flos Primulae
- Example 3 Herba Rumicis
- the respective germ output values are compared in the table below in comparison with the germ values after the disinfection according to the invention and the sterilization according to the prior art using the examples above.
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- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Medical Informatics (AREA)
- Mycology (AREA)
- Mechanical Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Alternative & Traditional Medicine (AREA)
- Biotechnology (AREA)
- Botany (AREA)
- Molecular Biology (AREA)
- Medicinal Chemistry (AREA)
- Microbiology (AREA)
- General Engineering & Computer Science (AREA)
- Natural Medicines & Medicinal Plants (AREA)
- Pharmacology & Pharmacy (AREA)
- Epidemiology (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Medicines Containing Plant Substances (AREA)
- Agricultural Chemicals And Associated Chemicals (AREA)
- Medicinal Preparation (AREA)
- Drying Of Solid Materials (AREA)
- Acyclic And Carbocyclic Compounds In Medicinal Compositions (AREA)
Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DK96943940T DK0868193T3 (da) | 1996-12-12 | 1996-12-12 | Fremgangsmåde til skånsom kimreducering af farmaceutiske tilberedninger |
US09/091,278 US6068816A (en) | 1995-12-21 | 1996-12-12 | Process for the mild reduction of germs in pharmaceutical preparations |
EP96943940A EP0868193B1 (de) | 1995-12-21 | 1996-12-12 | Verfahren zur schonenden keimreduzierung von pharmazeutischen zubereitungen |
AT96943940T ATE189605T1 (de) | 1995-12-21 | 1996-12-12 | Verfahren zur schonenden keimreduzierung von pharmazeutischen zubereitungen |
DE59604441T DE59604441D1 (de) | 1995-12-21 | 1996-12-12 | Verfahren zur schonenden keimreduzierung von pharmazeutischen zubereitungen |
AU13708/97A AU1370897A (en) | 1995-12-21 | 1996-12-12 | Process for gently sterilising pharmaceutical compositions |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19547973A DE19547973C2 (de) | 1995-12-21 | 1995-12-21 | Verfahren zur schonenden Keimreduzierung von pharmazeutischen Zubereitungen |
DE19547973.4 | 1995-12-21 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1997023232A1 true WO1997023232A1 (de) | 1997-07-03 |
Family
ID=7780905
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP1996/005578 WO1997023232A1 (de) | 1995-12-21 | 1996-12-12 | Verfahren zur schonenden keimreduzierung von pharmazeutischen zubereitungen |
Country Status (6)
Country | Link |
---|---|
US (1) | US6068816A (de) |
EP (1) | EP0868193B1 (de) |
AT (1) | ATE189605T1 (de) |
AU (1) | AU1370897A (de) |
DE (2) | DE19547973C2 (de) |
WO (1) | WO1997023232A1 (de) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1010461A1 (de) * | 1998-12-15 | 2000-06-21 | Bionorica Arzneimittel GmbH | Verfahren zur Herstellung von Arzneimittelvorprodukte für Tabletten, Pellets und Dragees |
US6306444B1 (en) * | 1998-12-15 | 2001-10-23 | Bionorica Arzneimittel Gmbh | Flowable drug precursor products ready for pressing for tablets, pellets and sugar-coated tablets and processes for preparing the same |
CN107441123A (zh) * | 2017-08-09 | 2017-12-08 | 芜湖振龙齐欣药业有限公司 | 一种破壁中药饮片的制备方法 |
CN111664661A (zh) * | 2020-06-03 | 2020-09-15 | 云南昊辰食品有限公司 | 一种不破坏当归有效成分的真空干燥方法 |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10112167C2 (de) * | 2001-03-12 | 2003-02-13 | Bionorica Ag | Verfahren zur schonenden Gewinnung von Trockenextrakten |
US8541399B2 (en) | 2002-02-19 | 2013-09-24 | Resolution Chemicals Limited | Solvent-based sterilisation of pharmaceuticals |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0435302A1 (de) * | 1989-12-29 | 1991-07-03 | Claude Blaizat | Verfahren und Einrichtung für teilweise oder völlige Deshydratierung von Pflanzenprodukten |
HU210015B (en) * | 1991-09-13 | 1995-07-28 | Szarvady | Process for producing antiflogistic plant extract |
EP0753306A1 (de) * | 1995-07-10 | 1997-01-15 | Plantamed Arzneimittel GmbH | Verfahren zur Herstellung von pharmazeutischen Zubereitungen mit höherem Gehalt an etherischen Ölen und Phenolen |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3868213A (en) * | 1973-10-25 | 1975-02-25 | Valery Petrovich Shulika | Vibration furnace |
DE2422907C2 (de) * | 1974-05-11 | 1986-04-03 | Fritz Lödige | Vorrichtung zum Sterilisieren von Schüttgütern |
DE2841067A1 (de) * | 1978-09-21 | 1980-03-27 | Werner Georg Munk | Verfahren zur herstellung von getrockneten, chipsartigen nahrungs- oder genussmittelscheiben |
US4876802A (en) * | 1983-12-21 | 1989-10-31 | Gerhard Gergely | Process and means for the heat treatment of powdery or granulate material |
US4844933A (en) * | 1986-10-30 | 1989-07-04 | Mccormick & Company, Inc. | Process for sterilization of spices and leafy herbs |
US5044091B1 (en) * | 1989-04-18 | 1997-12-30 | Sankyo Co | Method of preparing a freeze-dried formulation of a drug |
JP2514102B2 (ja) * | 1990-06-13 | 1996-07-10 | ユリカ株式会社 | ユリ科アロエ属に属する植物の真空凍結乾燥体を利用した錠剤製品及びその製造方法 |
DE4126138A1 (de) * | 1991-08-07 | 1993-02-11 | Andreas J R Trinkl | Verfahren zur erzielung einer natuerlichen umroetung und farberhaltung auf der basis natuerlicher gewuerze in weiterentwicklung auf der basis von gefriertrocknung (lyophilisierung) |
NO971716L (no) * | 1996-04-23 | 1997-10-24 | Atlas Stord Denmark A S | Fremgangsmåte og apparat til sterilisering og/eller varmebehandling av produkter i partikkelform, f.eks. kjöttbenmel, samt prosessanlegg til dette |
-
1995
- 1995-12-21 DE DE19547973A patent/DE19547973C2/de not_active Expired - Fee Related
-
1996
- 1996-12-12 US US09/091,278 patent/US6068816A/en not_active Expired - Fee Related
- 1996-12-12 WO PCT/EP1996/005578 patent/WO1997023232A1/de active IP Right Grant
- 1996-12-12 AU AU13708/97A patent/AU1370897A/en not_active Abandoned
- 1996-12-12 DE DE59604441T patent/DE59604441D1/de not_active Expired - Fee Related
- 1996-12-12 EP EP96943940A patent/EP0868193B1/de not_active Expired - Lifetime
- 1996-12-12 AT AT96943940T patent/ATE189605T1/de not_active IP Right Cessation
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0435302A1 (de) * | 1989-12-29 | 1991-07-03 | Claude Blaizat | Verfahren und Einrichtung für teilweise oder völlige Deshydratierung von Pflanzenprodukten |
HU210015B (en) * | 1991-09-13 | 1995-07-28 | Szarvady | Process for producing antiflogistic plant extract |
EP0753306A1 (de) * | 1995-07-10 | 1997-01-15 | Plantamed Arzneimittel GmbH | Verfahren zur Herstellung von pharmazeutischen Zubereitungen mit höherem Gehalt an etherischen Ölen und Phenolen |
Non-Patent Citations (1)
Title |
---|
DATABASE WPI Section Ch Week 9624, Derwent World Patents Index; Class B04, AN 96-233025, XP002029962 * |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1010461A1 (de) * | 1998-12-15 | 2000-06-21 | Bionorica Arzneimittel GmbH | Verfahren zur Herstellung von Arzneimittelvorprodukte für Tabletten, Pellets und Dragees |
US6306444B1 (en) * | 1998-12-15 | 2001-10-23 | Bionorica Arzneimittel Gmbh | Flowable drug precursor products ready for pressing for tablets, pellets and sugar-coated tablets and processes for preparing the same |
CN107441123A (zh) * | 2017-08-09 | 2017-12-08 | 芜湖振龙齐欣药业有限公司 | 一种破壁中药饮片的制备方法 |
CN111664661A (zh) * | 2020-06-03 | 2020-09-15 | 云南昊辰食品有限公司 | 一种不破坏当归有效成分的真空干燥方法 |
Also Published As
Publication number | Publication date |
---|---|
EP0868193B1 (de) | 2000-02-09 |
AU1370897A (en) | 1997-07-17 |
EP0868193A1 (de) | 1998-10-07 |
DE19547973C2 (de) | 1999-08-12 |
US6068816A (en) | 2000-05-30 |
ATE189605T1 (de) | 2000-02-15 |
DE59604441D1 (de) | 2000-03-16 |
DE19547973A1 (de) | 1997-06-26 |
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