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TW201517896A - System for producing microneedle pharmaceutical preparation, and air-conditioning method - Google Patents

System for producing microneedle pharmaceutical preparation, and air-conditioning method Download PDF

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Publication number
TW201517896A
TW201517896A TW103118824A TW103118824A TW201517896A TW 201517896 A TW201517896 A TW 201517896A TW 103118824 A TW103118824 A TW 103118824A TW 103118824 A TW103118824 A TW 103118824A TW 201517896 A TW201517896 A TW 201517896A
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air
humidity
temperature
microneedle
coating chamber
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TWI636781B (en
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Shinpei Nishimura
Toshiyuki Matsudo
Seiji Tokumoto
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Hisamitsu Pharmaceutical Co
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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61MDEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M37/00Other apparatus for introducing media into the body; Percutany, i.e. introducing medicines into the body by diffusion through the skin
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61MDEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M37/00Other apparatus for introducing media into the body; Percutany, i.e. introducing medicines into the body by diffusion through the skin
    • A61M37/0015Other apparatus for introducing media into the body; Percutany, i.e. introducing medicines into the body by diffusion through the skin by using microneedles
    • A61M2037/0023Drug applicators using microneedles
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61MDEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M37/00Other apparatus for introducing media into the body; Percutany, i.e. introducing medicines into the body by diffusion through the skin
    • A61M37/0015Other apparatus for introducing media into the body; Percutany, i.e. introducing medicines into the body by diffusion through the skin by using microneedles
    • A61M2037/0046Solid microneedles
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61MDEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
    • A61M37/00Other apparatus for introducing media into the body; Percutany, i.e. introducing medicines into the body by diffusion through the skin
    • A61M37/0015Other apparatus for introducing media into the body; Percutany, i.e. introducing medicines into the body by diffusion through the skin by using microneedles
    • A61M2037/0053Methods for producing microneedles

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  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Dermatology (AREA)
  • Medical Informatics (AREA)
  • Anesthesiology (AREA)
  • Biomedical Technology (AREA)
  • Heart & Thoracic Surgery (AREA)
  • Hematology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • Media Introduction/Drainage Providing Device (AREA)

Abstract

The present invention is a system for producing a microneedle pharmaceutical preparation by coating a microneedle with a coating liquid containing a drug, and adjusting the atmospheric environment in the coating chamber for producing the microneedle pharmaceutical preparation, the system for producing the microneedle pharmaceutical preparation being equipped with: an air compressor; a moisture-permeable-film-type humidity adjustment device for adjusting the humidity of the air supplied by an air compressor, and separating the air and the water content serving as the humidity adjustment source with a moisture-permeable film; a pressure adjustment device for adjusting the pressure of the air to be supplied by the air compressor; and an air filter for removing bacteria from the air supplied to the interior of the coating chamber.

Description

微針製劑製造用系統及空調方法 Microneedle preparation manufacturing system and air conditioning method

本發明為關於一種用於將藥劑塗布於微針上來製造微針製劑之系統及空調方法。 The present invention relates to a system for producing a microneedle preparation for applying a medicament to a microneedle and an air conditioning method.

作為用於提升藥劑的經皮吸收之手法,被熟知有微針製劑。將藥劑塗布於微針製劑之微針上的方法,有所謂的浸漬方式(例如,專利文獻1)。此為,於形成於屏障板上的複數個開口部中,填充包含藥劑之塗布液,將微針插入其開口部,並將塗布液塗布於微針上之方法。藉由此方法,能夠於微針上塗布一定量的塗布液。 As a method for enhancing transdermal absorption of a drug, a microneedle preparation is known. A method of applying a drug to a microneedle of a microneedle preparation has a so-called immersion method (for example, Patent Document 1). This is a method in which a coating liquid containing a drug is filled in a plurality of openings formed on the barrier plate, a microneedle is inserted into the opening, and a coating liquid is applied to the microneedle. By this method, a certain amount of the coating liquid can be applied to the microneedles.

[先前技術文獻] [Previous Technical Literature] [專利文獻] [Patent Literature]

[專利文獻1]國際公開第2008/139648號 [Patent Document 1] International Publication No. 2008/139648

然而,作為塗布液中之溶媒,使用水時,即 使使用專利文獻1所揭示之方法來進行塗布,在將塗布液塗布於微針後,檢查經過乾燥步驟所得之微針製劑之微針上的藥劑量,得知隨著製造日期或製造時間等會發生不均勻,要安定地製造是相當困難的。 However, when water is used as a solvent in the coating liquid, Coating is carried out by the method disclosed in Patent Document 1, and after applying the coating liquid to the microneedles, the amount of the drug on the microneedles of the microneedle preparation obtained by the drying step is examined, and it is known that the manufacturing date or the manufacturing time is the same. Unevenness will occur, and it is quite difficult to manufacture stably.

於此,本發明者們為了防止塗布於微針上之 藥劑量的不均勻,鎖定對微針進行藥劑塗布之塗布腔室內的環境,並發現藉由將塗布腔室內設定在特定範圍之溫度及濕度,抑制塗布液的物性變化,藉此,抑制塗布於微針上之藥劑量的不均勻。 Here, the inventors have tried to prevent application to the microneedles. The unevenness of the amount of the drug is used to lock the environment in the coating chamber where the microneedle is coated with the drug, and it is found that the physical properties of the coating liquid are suppressed by setting the coating chamber within a specific range of temperature and humidity, thereby suppressing application to the coating liquid. The amount of the drug on the microneedle is not uniform.

然而,藉由於塗布腔室之內部設置溫度調節 裝置及調濕器,來直接控制塗布腔室內的溫濕度是相當困難的。於此,本發明者們思及,藉由將於塗布腔室之外部預先調節至特定範圍之溫度及濕度的空氣供給於塗布腔室內,來將塗布腔室內維持在所期望之溫濕度之手段,而達成本發明。 However, due to the internal temperature setting of the coating chamber It is quite difficult to directly control the temperature and humidity in the coating chamber by means of the device and the humidity controller. Here, the inventors of the present invention have thought that the air in the coating chamber can be maintained at a desired temperature and humidity by supplying air having a temperature and a humidity which is adjusted to a specific range outside the coating chamber to the coating chamber. The invention is achieved.

且,如以上所述,欲藉由調節塗布腔室內之 溫濕度,來抑制塗布液之物性變化時,根據塗布液之組成,必需要比較高的濕度。另一方面,微針製劑必需要在無菌狀態下製造。通常,為了將某空間呈現無菌狀態,會採用將濕度下降而抑制微生物繁殖之手段,故認為在微針製劑製造用系統中,以往要同時實現高濕度與無菌狀態之兩個相反狀態是相當困難的。 And, as described above, to adjust the coating chamber When the temperature and humidity are used to suppress the change in the physical properties of the coating liquid, it is necessary to have a relatively high humidity depending on the composition of the coating liquid. On the other hand, microneedle preparations must be manufactured under aseptic conditions. In general, in order to sterilize a certain space, a means of reducing the humidity and inhibiting the growth of microorganisms is employed. Therefore, it is considered that in the system for manufacturing a microneedle preparation, it is quite difficult to simultaneously achieve two opposite states of high humidity and sterilized state. of.

然而,本發明者們發現,藉由採用將於塗布 腔室之外部預先調整至特定範圍之溫度及濕度的空氣供給於塗布腔室內之手段,即能夠充分地滿足此相反的要求。 However, the inventors have found that by using a coating that will be applied The means for externally adjusting the temperature of the outside of the chamber to a specific range of temperature and humidity to be supplied into the coating chamber sufficiently satisfies the opposite requirement.

圖1為基於上述著眼點,而由本發明者們所 思考出的微針製劑製造用系統之一示例。圖1所示之微針製劑製造用100,係具備空氣壓縮機10、與調節由空氣壓縮機10所供給之空氣的溫度之壓縮空氣溫度調節裝置12、與調節溫度經壓縮空氣溫度調節裝置12所調節之空氣的濕度之濕度調節裝置18、與將供給至塗布腔室內的空氣除菌之空氣過濾器16。藉由使用具有如此構成之系統100,將已預先調節成特定範圍之溫度及濕度的無菌狀態之空氣供給於塗布腔室內,能夠將塗布腔室內維持在所期望的空氣環境。塗布腔室內之空氣環境為特定範圍之溫度及濕度時,能夠抑制塗布腔室內之塗布液的物性變化,因此在該環境下,被塗布於微針上的藥劑量之不均勻也會被抑制。 Figure 1 is based on the above points of view, and is invented by the present inventors. An example of a system for the manufacture of microneedle preparations to be considered. The microneedle preparation manufacturing 100 shown in Fig. 1 is provided with an air compressor 10, a compressed air temperature adjusting device 12 for adjusting the temperature of the air supplied from the air compressor 10, and a compressed air temperature adjusting device 12 for adjusting the temperature. The humidity adjusting device 18 for adjusting the humidity of the air and the air filter 16 for sterilizing the air supplied into the coating chamber. By using the system 100 having such a configuration, air in an aseptic state that has been previously adjusted to a specific range of temperature and humidity is supplied into the coating chamber, whereby the coating chamber can be maintained in a desired air environment. When the air environment in the coating chamber is a specific range of temperature and humidity, the physical property change of the coating liquid in the coating chamber can be suppressed. Therefore, in this environment, the unevenness of the amount of the drug applied to the microneedles is also suppressed.

另一方面,因為塗布於微針製劑上的塗布液 之組成的不同,為了抑制塗布液之物性變化,有時必須要將塗布腔室內設成30~70%(RH)之濕度(中濕度)。然而得知,使用具有上述構成之系統100,即使能夠調節成超過70%(RH)之濕度(高濕度),要精準地調節成比此更低之範圍的濕度並維持是較困難的。 On the other hand, because of the coating liquid applied to the microneedle preparation In order to suppress the change in the physical properties of the coating liquid, it is necessary to set the coating chamber to a humidity (medium humidity) of 30 to 70% (RH). However, it has been found that with the system 100 having the above configuration, even if it can be adjusted to a humidity (high humidity) exceeding 70% (RH), it is difficult to accurately adjust the humidity to a lower range and maintain it.

於此,本發明之目的為提供一種微針製劑製 造用系統及空調方法,其係能夠將對微針進行藥劑塗布之塗布腔室內的空氣環境調節成30~70%(RH)之中濕度。 Herein, the object of the present invention is to provide a microneedle preparation system. The manufacturing system and the air conditioning method are capable of adjusting the air environment in the coating chamber where the microneedle is coated with the drug to a humidity of 30 to 70% (RH).

為了達成上述目的,本發明為提供一種微針製劑製造用系統,其係用於將包含藥劑之塗布液塗布於微針來製造微針製劑,且調節塗布腔室內之空氣環境的微針製劑製造用系統,並具備:空氣壓縮機、與用來調節由空氣壓縮機所供給之空氣的濕度,且空氣與作為濕度調節源的水分會被透濕膜分離之透濕膜型的濕度調節裝置、與調節由空氣壓縮機所供給之空氣的壓力之壓力調節裝置、與將供給至該塗布腔室內的空氣除菌之空氣過濾器。 In order to achieve the above object, the present invention provides a system for producing a microneedle preparation for applying a coating liquid containing a pharmaceutical agent to a microneedle to manufacture a microneedle preparation, and adjusting a microneedle preparation for an air environment in a coating chamber. The system includes: an air compressor, a humidity-permeable membrane type humidity adjusting device for adjusting the humidity of the air supplied by the air compressor, and the air and the moisture as a humidity adjusting source are separated by the moisture permeable membrane, And a pressure adjusting device that adjusts the pressure of the air supplied by the air compressor, and an air filter that sterilizes the air supplied into the coating chamber.

將具有如此構成之微針製劑製造用系統在溫度為特定範圍內之環境下使用,藉由調節流通於透濕膜型之濕度調節裝置內的流路之空氣的壓力,能夠將控制在30~70%(RH)之範圍的任意濕度,且為無菌狀態的空氣安定地供給至塗布腔室內。 The system for producing a microneedle preparation having such a configuration is used in an environment having a temperature within a specific range, and the pressure of the air flowing through the flow path in the moisture permeable membrane type humidity control device can be controlled at 30~. Any humidity in the range of 70% (RH), and the sterilized air is stably supplied into the coating chamber.

上述透濕膜能夠使用形成為中空纖絲狀者。透濕膜藉由形成為中空纖絲狀,能夠更有效率地進行濕度調節。 The moisture permeable film can be formed into a hollow fibril. The moisture permeable film is formed into a hollow fibril shape, and humidity adjustment can be performed more efficiently.

微針製劑製造用系統為具備濕度探測器、與基於對應於前述濕度探測器所檢測出的濕度之信號,來控制壓力調節裝置之第1控制手段較佳。且,微針製劑製造用系統亦可具備溫度探測器、與基於對應於溫度探測器所檢測出的溫度之信號,來控制壓力調節裝置之第2控制手段。藉由如此來設置第1控制手段及/或第2控制手段, 能夠因應塗布腔室內的溫濕度,而隨時操控壓力調節裝置,並能夠更有效率,且確實地來控制塗布腔室內之溫濕度。 The system for producing a microneedle preparation is preferably a first control means including a humidity detector and a signal for controlling the pressure adjusting means based on a signal corresponding to the humidity detected by the humidity detector. Further, the microneedle preparation system may be provided with a temperature detector and a second control means for controlling the pressure adjustment means based on a signal corresponding to the temperature detected by the temperature detector. By providing the first control means and/or the second control means in this manner, The pressure regulating device can be operated at any time in response to the temperature and humidity in the coating chamber, and the temperature and humidity in the coating chamber can be controlled more efficiently and reliably.

微針製劑製造用系統亦可具備調節由空氣壓 縮機所供給之空氣的溫度之壓縮空氣溫度調節裝置。配置系統之環境的溫度有變動,且因為空氣壓縮機而無法使提供至系統內的空氣為所期望之範圍之溫度時,系統藉由具備壓縮空氣溫度調節裝置,而能夠將送入塗布腔室內之空氣調節成任意之溫度,且能夠更精確地來進行濕度的控制。 The system for manufacturing microneedle preparations can also be adjusted by air pressure A compressed air temperature regulating device that reduces the temperature of the air supplied by the machine. When the temperature of the environment in which the system is configured varies, and the air supplied to the system is not within the desired range due to the air compressor, the system can be fed into the coating chamber by providing a compressed air temperature adjusting device. The air is regulated to an arbitrary temperature, and the humidity can be controlled more accurately.

微針製劑製造用系統亦可具備濕度探測器與 第3控制手段較佳,該第3控制手段為,基於對應於以濕度探測器所檢測出的濕度之信號,來控制壓縮空氣溫度調節裝置。另外,微針製劑製造用系統亦可具備溫度探測器與第4控制手段,該第4控制手段為,基於對應於以溫度探測器所檢測出的溫度之信號,來控制壓縮空氣溫度調節裝置。藉由如此設置第3控制手段及/或第4控制手段,能夠因應塗布腔室內的溫濕度,來隨時操作壓縮空氣溫度調節裝置,並能夠更有效率,且確實地來控制塗布腔室內之溫濕度。 The microneedle preparation system can also be equipped with a humidity detector and Preferably, the third control means controls the compressed air temperature adjusting means based on a signal corresponding to the humidity detected by the humidity detector. Further, the system for producing a microneedle preparation may further include a temperature detector and a fourth control means for controlling the compressed air temperature adjusting means based on a signal corresponding to the temperature detected by the temperature detector. By providing the third control means and/or the fourth control means in this manner, the compressed air temperature adjusting device can be operated at any time in accordance with the temperature and humidity in the coating chamber, and the temperature in the coating chamber can be controlled more efficiently and reliably. humidity.

濕度調節裝置具備供給水分之水分供給器較 適合。濕度調節裝置藉由具有如此之構成,能夠簡單地供應調節系統內之濕度所用的水分。 The humidity regulator has a water supply device for supplying moisture Suitable for. With such a configuration, the humidity control device can easily supply the moisture for adjusting the humidity in the system.

且,水分供給器為恆溫水槽較佳。藉由將恆 溫水槽作為水分供給器使用,由於能夠將水分供給器之水分容易地保持在一定的溫度下,故能夠高精度地來進行溫濕度之控制。 Further, the moisture supplier is preferably a constant temperature water tank. By being constant Since the warm water tank is used as a water supply device, the moisture of the moisture supplier can be easily maintained at a constant temperature, so that the temperature and humidity can be controlled with high precision.

且,水分供給器為能夠調節水溫者,亦即, 在具有幅度的溫度範圍中,能夠調節成任意之溫度者為有效。水分供給器藉由具有如此之機能,能夠將水分供給器之水分保持在幅度廣之範圍中的任意之一定溫度。 Moreover, the moisture supplier is a person capable of adjusting the water temperature, that is, In the temperature range having the amplitude, it can be effective to adjust to any temperature. By having such a function, the moisture supplier can maintain the moisture of the moisture supplier at any constant temperature in a wide range.

微針製劑製造用系統亦可具備濕度探測器、 與基於對應於濕度探測器所檢測出的濕度之信號,來控制水分供給器之水溫的第5控制手段。且,微針製劑製造用系統亦可具備溫度探測器、與基於對應於溫度探測器所檢測出的溫度之信號,來控制水分供給器之水溫控制的第6控制手段。藉由如此來設置第5控制手段及/或第6控制手段,能夠因應塗布腔室內之溫濕度,而隨時操控水分供給器之水溫,並能夠更有效、且更確實地來控制塗布腔室內之溫濕度。 The microneedle preparation system can also be equipped with a humidity detector, And a fifth control means for controlling the water temperature of the moisture supplier based on a signal corresponding to the humidity detected by the humidity detector. Further, the system for producing a microneedle preparation may further include a temperature detector and a sixth control means for controlling the water temperature control of the moisture supplier based on a signal corresponding to the temperature detected by the temperature detector. By providing the fifth control means and/or the sixth control means in this manner, the water temperature of the water supply device can be manipulated at any time in accordance with the temperature and humidity in the coating chamber, and the coating chamber can be controlled more effectively and more reliably. Temperature and humidity.

藉由本發明之其他態樣,係提供一種空調方 法,其係用於將包含藥劑之塗布液塗布於微針,來製造微針製劑,且用於調節塗布腔室內之空氣環境之空調方法,其包含:以前述空氣與作為濕度調節源之水分會被透濕膜所分離之透濕膜型的濕度調節裝置來調節送入塗布腔室之空氣的濕度之步驟、與藉由壓力調節裝置來調節送入該塗布腔室之空氣的壓力之步驟、與藉由空氣過濾器來除菌前述空氣之步驟、與將經濕度調節且經除菌之空氣導入塗布 腔室內之步驟。 By other aspects of the invention, an air conditioner is provided The method for applying a coating liquid containing a drug to a microneedle to manufacture a microneedle preparation, and an air conditioning method for adjusting an air environment in a coating chamber, comprising: the air and the moisture as a humidity adjustment source a moisture permeable membrane type humidity adjusting device which is separated by a moisture permeable membrane to adjust the humidity of the air supplied to the coating chamber, and a step of adjusting the pressure of the air supplied to the coating chamber by the pressure adjusting means And the step of sterilizing the air by means of an air filter, and introducing the humidity-conditioned and sterilized air into the coating The steps in the chamber.

以如此之空調方法,再藉由將溫度為特定範 圍內之空氣供給至濕度調節裝置中,能夠將溫度在所期望之範圍,且被控制在30~70%(RH)之範圍中之任意濕度的無菌狀態之空氣安定地供給至塗布腔室內。 With such an air conditioning method, by using the temperature as a specific The air in the enclosure is supplied to the humidity control device, and the sterilized air having a temperature within a desired range and controlled to any humidity in the range of 30 to 70% (RH) can be stably supplied into the coating chamber.

藉由本發明之微針製劑製造用系統或空調方法,能夠將所期望範圍之溫度及被設成30~70%(RH)之範圍之任意濕度,且為無菌狀態之空氣安定地供給至塗布腔室內。藉此,不會被塗布腔室內外的溫濕度的日後及日內之變動所影響,能夠將塗布腔室內維持在所期望範圍的溫濕度,故能夠抑制塗布腔室內的塗布液物性之變動。因此,藉由本發明之微針製劑製造用系統或空調方法,在經調節之空氣環境下來將包含藥劑之塗布液塗布於微針上的話,能夠安定地製造塗布有一定藥劑量的微針製劑。 According to the system for producing a microneedle preparation of the present invention or the air conditioning method, it is possible to stably supply the temperature in a desired range and any humidity in a range of 30 to 70% (RH) to the coating chamber in a sterile state. indoor. Thereby, the temperature and humidity of the coating chamber can be maintained within a desired range without being affected by fluctuations in the temperature and humidity inside and outside the coating chamber, and the fluctuation of the physical properties of the coating liquid in the coating chamber can be suppressed. Therefore, according to the system for producing a microneedle preparation of the present invention or the air conditioning method, when a coating liquid containing a drug is applied to a microneedle in an adjusted air atmosphere, a microneedle preparation coated with a certain amount of a drug can be stably produced.

10‧‧‧空氣壓縮機 10‧‧‧Air compressor

12‧‧‧壓縮空氣溫度調節裝置 12‧‧‧Compressed air temperature regulator

14‧‧‧風量調節裝置 14‧‧‧Air volume adjustment device

16‧‧‧空氣過濾器 16‧‧‧Air filter

18‧‧‧濕度調節裝置 18‧‧‧Humidity control device

20‧‧‧塗布腔室 20‧‧‧ Coating chamber

21‧‧‧開口 21‧‧‧ openings

22‧‧‧水分供給器 22‧‧‧Water supply

23‧‧‧透濕膜 23‧‧‧Translucent membrane

24‧‧‧透濕膜裝置 24‧‧ ‧ wet film device

26‧‧‧溫濕度探測器(溫度探測器及濕度探測器) 26‧‧‧ Temperature and Humidity Detector (Temperature Detector and Humidity Detector)

28‧‧‧控制裝置(第1~第6控制手段) 28‧‧‧Control device (1st to 6th control means)

30‧‧‧壓力調節裝置 30‧‧‧ Pressure regulating device

40‧‧‧微針製劑 40‧‧‧Microneedle preparation

42‧‧‧基板 42‧‧‧Substrate

44‧‧‧微針 44‧‧‧microneedle

46‧‧‧塗布層 46‧‧‧coating layer

50‧‧‧塗布液 50‧‧‧ Coating solution

52‧‧‧屏障板 52‧‧‧Barrier board

54‧‧‧刮勺 54‧‧‧Scrape

56‧‧‧開口部 56‧‧‧ openings

100、200‧‧‧微針製劑製造用系統 100,200‧‧‧Microneedle preparation system

L‧‧‧送風管線 L‧‧‧Air supply line

[圖1]表示微針製劑製造用系統之一實施形態之方塊流程圖。 Fig. 1 is a block flow chart showing an embodiment of a system for producing a microneedle preparation.

[圖2]表示微針製劑製造用系統之一實施形態之方塊流程圖。 Fig. 2 is a block flow chart showing an embodiment of a system for producing a microneedle preparation.

[圖3]表示微針製劑製造用系統中濕度調節裝置之一 實施形態之模式的剖面圖。 [Fig. 3] shows one of humidity adjusting devices in a system for manufacturing a microneedle preparation A cross-sectional view of a mode of the embodiment.

[圖4]表示微針製劑之一例的斜視圖。 Fig. 4 is a perspective view showing an example of a microneedle preparation.

[圖5]圖4之微針製劑之V-V線剖面圖。 Fig. 5 is a cross-sectional view taken along the line V-V of the microneedle preparation of Fig. 4.

[圖6](a)~(c)表示微針製劑之製造方法之一例的模式圖。 Fig. 6 (a) to (c) are schematic views showing an example of a method for producing a microneedle preparation.

[圖7](a)~(c)表示塗布腔室內之濕度變化之圖形。 [Fig. 7] (a) to (c) are graphs showing changes in humidity in the coating chamber.

[圖8]表示塗布於微針上之藥劑的含量之圖形。 Fig. 8 is a graph showing the content of a drug applied to a microneedle.

[圖9]表示風量調節試驗用之塗布腔室的模式斜視圖。 Fig. 9 is a schematic perspective view showing a coating chamber for an air volume adjustment test.

[圖10](a)表示塗布腔室內之溫度變化的圖形,(b)表示塗布腔室內之濕度變化的圖形。 Fig. 10 (a) is a graph showing a temperature change in a coating chamber, and (b) is a graph showing a change in humidity in a coating chamber.

[圖11](a)表示塗布腔室內之溫度變化的圖形,(b)表示塗布腔室內之濕度變化的圖形。 Fig. 11 (a) is a graph showing a change in temperature in a coating chamber, and (b) is a graph showing a change in humidity in a coating chamber.

[實施發明之形態] [Formation of the Invention]

以下,一邊參照圖示,一邊針對本發明之微針製劑製造用系統及空調方法之較佳實施形態來進行說明。且,圖中,對相同或部分相同附上相同符號,並省略其詳細說明。 Hereinafter, preferred embodiments of the microneedle preparation system and the air conditioning method of the present invention will be described with reference to the drawings. In the drawings, the same reference numerals are given to the same or parts, and the detailed description is omitted.

本實施形態相關之微針製劑製造用系統(以下,有時亦單純稱作「系統」。)為作出一種空氣環境,其係適合於進行將包含藥劑之塗布液塗布於微針來製造微 針製劑之作業。本說明書中,濕度意指相對濕度。 The system for producing a microneedle preparation according to the present embodiment (hereinafter sometimes referred to simply as "system") is an air environment suitable for applying a coating liquid containing a drug to a microneedle to produce micro The operation of the needle preparation. In this specification, humidity means relative humidity.

圖2為,表示本發明之微針製劑製造用系統 之一實施形態之方塊流程圖。微針製劑製造用系統200中之構成為:空氣壓縮機10、壓縮空氣溫度調節裝置12、壓力調節裝置30、濕度調節裝置18、風量調節裝置14及空氣過濾器16分別依此順序介隔送風管線L來連接。送風管線L的終點連接於配置有微針且進行藥劑之塗布的塗布腔室20。 2 is a view showing a system for producing a microneedle preparation of the present invention A block flow diagram of one embodiment. The system for manufacturing the microneedle preparation system 200 is configured such that the air compressor 10, the compressed air temperature adjusting device 12, the pressure adjusting device 30, the humidity adjusting device 18, the air volume adjusting device 14, and the air filter 16 respectively separate the air supply in this order. Line L is connected. The end point of the air supply line L is connected to the coating chamber 20 in which the microneedles are disposed and the application of the drug is performed.

接著,針對本實施形態相關之微針製劑製造用系統200的各構成來進行說明。 Next, each configuration of the system for producing a microneedle preparation according to the present embodiment will be described.

本實施形態相關之微針製劑製造用系統200中的空氣壓縮機10,只要是能夠產生所期望之風速(流速)的氣流即可,空氣壓縮機10之壓縮比並無特別限制。因此,作為空氣壓縮機10,並非限定於JIS(B 0132:2005)所規定之壓縮機,能夠使用壓縮比較低的送風機等。由空氣壓縮機10供給至本系統200內之空氣的風量為10~250L/min較佳,以20~100L/min更佳。且,風量亦可為0.3~10L/min。被供給之空氣的風量,能夠當作塗布腔室20之每容積中的風量來計算。供給至塗布腔室20之每容積1L中的空氣之風量為28~696L/min較佳,為56~278L/min更佳。且,供給至塗布腔室20之每容積1L中的空氣之風量亦可為1~28L/min。且,作為由空氣壓縮機10供給至本系統200內的空氣,雖然能夠使用存在於系統外部之空氣,但因應塗布於微針上的塗布液之組 成,亦可混合任意氣體。 The air compressor 10 in the system for producing a microneedle preparation according to the present embodiment is not particularly limited as long as it can generate a desired air velocity (flow velocity). Therefore, the air compressor 10 is not limited to the compressor defined by JIS (B 0132:2005), and a blower having a relatively low compression can be used. The air volume supplied from the air compressor 10 to the air in the system 200 is preferably from 10 to 250 L/min, more preferably from 20 to 100 L/min. Moreover, the air volume can also be 0.3~10L/min. The amount of air supplied to the air can be calculated as the amount of wind in each volume of the coating chamber 20. The air volume supplied to the coating chamber 20 in 1 L per volume is preferably 28 to 696 L/min, more preferably 56 to 278 L/min. Further, the amount of air supplied to the coating chamber 20 in 1 L per volume may be 1 to 28 L/min. Further, as the air supplied to the system 200 by the air compressor 10, although the air existing outside the system can be used, the group of the coating liquid applied to the microneedles is required. It can also be mixed with any gas.

本實施形態相關之微針製劑製造用系統200 中的壓縮空氣溫度調節裝置12,能夠將以空氣壓縮機10而從外部供給至本系統200內的空氣之溫度,調節成任意之溫度。因此,即使本系統200的外部空氣之溫度有日後及日內之變動時,藉由設置壓縮空氣溫度調節裝置12,不因外部環境而能夠將流通於本系統200內之空氣的溫度維持在所期望之範圍內。壓縮空氣溫度調節裝置12中,作為注入於壓縮空氣溫度調節裝置12內之空氣的溫度,適應於約5~40℃之範圍較佳。由壓縮空氣溫度調節裝置12送入下游側之送風管線L的空氣之溫度,因應所使用之塗布液的組成,能夠任意地設定,但以溫度調節之效率觀點來說,設定在室溫附近較佳,設定在20~30℃更佳。 且,使用能夠將排出空氣之溫度控制在±0.5℃以下之精準度的壓縮空氣溫度調節裝置12較佳。作為壓縮空氣溫度調節裝置12,只要是能夠精準度好地來控制壓縮空氣之溫度者即可,能夠使用溫度控制方式、放冷方式等所成者。 The microneedle preparation manufacturing system 200 according to the embodiment The compressed air temperature adjusting device 12 can adjust the temperature of the air supplied from the outside to the system 200 by the air compressor 10 to an arbitrary temperature. Therefore, even if the temperature of the outside air of the system 200 is changed in the future and in the daytime, by providing the compressed air temperature adjusting device 12, the temperature of the air flowing through the system 200 can be maintained at a desired level without the external environment. Within the scope. In the compressed air temperature adjusting device 12, the temperature of the air injected into the compressed air temperature adjusting device 12 is preferably in the range of about 5 to 40 °C. The temperature of the air sent to the downstream air supply line L by the compressed air temperature adjusting device 12 can be arbitrarily set depending on the composition of the coating liquid to be used, but it is set at around room temperature from the viewpoint of efficiency of temperature adjustment. Good, set at 20~30 °C is better. Further, it is preferable to use the compressed air temperature adjusting device 12 capable of controlling the temperature of the exhaust air to be ±0.5 ° C or less. As the compressed air temperature adjusting device 12, any temperature control method, cooling method, or the like can be used as long as the temperature of the compressed air can be accurately controlled.

本實施形態相關之微針製劑製造用系統200中的濕度調節裝置18,藉由組合上述之壓縮空氣溫度調節裝置12來使用,能夠將本系統200內所流通的空氣,調節成所期望之濕度,特別是30~70%(RH)之範圍的濕度並維持。濕度調節裝置18為透濕膜型,且具有包含形成為中空纖絲狀之透濕膜的透濕膜裝置24。如此之透濕 膜型的濕度調節裝置18,亦可具備供給水分之水分供給器22。作為透濕膜,例如,能夠使用將離子交換樹脂成形成中空纖絲狀者。透濕膜具有使水蒸氣通過,但不使液體之水通過之性質。 The humidity adjusting device 18 in the microneedle preparation system 200 according to the present embodiment can be used by combining the above-described compressed air temperature adjusting device 12, and the air flowing through the system 200 can be adjusted to a desired humidity. In particular, the humidity in the range of 30 to 70% (RH) is maintained. The humidity control device 18 is of a moisture permeable film type and has a moisture permeable film device 24 including a moisture permeable film formed into a hollow fiber shape. So wet The membrane type humidity controller 18 may further include a moisture supplier 22 that supplies moisture. As the moisture permeable film, for example, an ion exchange resin can be used to form a hollow fibril. The moisture permeable film has a property of allowing water vapor to pass therethrough without passing water of the liquid.

水分供給器22,為了控制一定的水溫,使用 恆溫水槽為有效。且,恆溫水槽能夠調節成具有幅度的溫度範圍,並能夠高精準度地調整成任意之溫度較佳。水分供給器22中所使用的水,為了確保其無菌狀態,為純水較佳。由水分供給器22供給至透濕膜裝置24的水分,介隔著透濕膜,作為被氣化之水蒸氣而供給至本系統200內。 The water supplier 22 is used to control a certain water temperature. The constant temperature water tank is effective. Moreover, the constant temperature water tank can be adjusted to have a temperature range of amplitude, and can be adjusted to any temperature with high precision. The water used in the moisture supplier 22 is preferably pure water in order to ensure its sterility. The moisture supplied to the moisture permeable membrane device 24 by the moisture supplier 22 is interposed between the moisture permeable membrane and supplied to the system 200 as vaporized vapor.

作為透濕膜裝置24,以效率性之觀點來看, 使用形成為中空纖絲狀之透濕膜被固定成多數束狀的中空纖絲模組較佳。使用中空纖絲模組時,為了使流通於本系統200內的空氣可以通過中空纖絲狀透濕膜的內部,將中空纖絲模組連接於本系統200之送風管線L上。且,中空纖絲狀透濕膜之外部構成為:使經水分供給器22,較佳為經恆溫水槽控制水溫的水連接而流通,並時常循環在中空纖絲狀透濕膜與水分供給器22之間較佳。介隔著中空纖絲狀透濕膜,一定溫度的水分與特定範圍之溫度的氣體接觸時,特定範圍之濕度的氣體會被中空纖絲模組而導出。因此,經壓縮空氣溫度調節裝置12而調節溫度之空氣會被導入中空纖絲模組中,且來自恆溫水槽之一定溫度的純水藉由通過中空纖絲模組,能使來自中空纖絲模組的 空氣具有所期望範圍之濕度,並流往下游。且,藉由控制恆溫水槽等水分供給器22的水溫,能夠高精準度地來進行濕度之控制。亦即,藉由將水溫上升至某個溫度,能夠將流通於本系統200內的空氣加濕至對應其溫度的濕度,相反地藉由將水溫降低至某個溫度,能夠將流通於本系統200內的空氣除濕至對應其溫度之濕度。另外,使用具有中空纖絲模組之透濕膜裝置24時,由於在中空纖絲模組中具有過濾器機能,有可能包含在水分供給器22中之水的微生物可以藉由中空纖絲模組而被捕捉,並能夠抑制其混入流通於本系統200內之空氣中。 As the moisture permeable membrane device 24, from the viewpoint of efficiency, It is preferable to use a hollow fiber module in which a moisture-permeable film formed into a hollow fiber shape is fixed in a plurality of bundles. When the hollow fiber module is used, the hollow fiber module is connected to the air supply line L of the system 200 so that the air flowing through the system 200 can pass through the inside of the hollow fiber-like moisture permeable film. Further, the outside of the hollow fiber-shaped moisture permeable membrane is configured such that the water supply device 22, preferably water which is controlled by the constant temperature water tank to control the water temperature, is circulated, and is often circulated in the hollow fiber-like moisture permeable membrane and the water supply. Preferably, the devices 22 are between each other. When a hollow fiber-like moisture permeable membrane is interposed between a certain temperature of a certain temperature, a gas of a specific range of humidity is derived by the hollow fiber module. Therefore, the air whose temperature is adjusted by the compressed air temperature adjusting device 12 is introduced into the hollow fiber module, and the pure water from a certain temperature of the constant temperature water tank can pass through the hollow fiber module to obtain the hollow fiber mold. Group The air has a desired range of humidity and flows downstream. Further, by controlling the water temperature of the water supplier 22 such as the constant temperature water tank, the humidity can be controlled with high precision. That is, by raising the temperature of the water to a certain temperature, the air flowing through the system 200 can be humidified to a humidity corresponding to the temperature, and conversely, by lowering the temperature of the water to a certain temperature, it can be circulated. The air in the system 200 is dehumidified to a humidity corresponding to its temperature. Further, when the moisture permeable membrane device 24 having the hollow fiber module is used, since the filter function is provided in the hollow fiber module, it is possible that the microorganisms contained in the water in the moisture supplier 22 can be made by the hollow fiber mold. The group is captured and can be prevented from being mixed into the air flowing through the system 200.

本實施形態相關之微針製劑製造用系統200 中壓力調節裝置30為能夠調節上述透濕膜裝置24之中空纖絲狀之透濕膜內部的壓力者。壓力調節裝置30被設置在壓縮空氣溫度調節裝置12之下游且透濕膜裝置24之上游。本系統200中,由於透濕膜裝置24之透濕膜被形成為中空纖絲狀,故藉由以壓力調節裝置30來調節導入該透濕膜裝置24中的空氣壓力,能夠調節由透濕膜裝置24所導出之空氣的濕度,特別是適合將塗布腔室內之濕度調節成約30~70%(RH)之中程度之濕度。作為壓力調節裝置30,只要是能夠精準地調節壓力即可,例如能夠使用隔膜式者。作為壓力調節裝置30,能夠使用能夠在0.02~1.0MPa之範圍下調壓者。 The microneedle preparation manufacturing system 200 according to the embodiment The medium pressure adjusting device 30 is a person capable of adjusting the pressure inside the hollow fibrillar moisture permeable membrane of the moisture permeable membrane device 24. The pressure regulating device 30 is disposed downstream of the compressed air temperature adjusting device 12 and upstream of the moisture permeable membrane device 24. In the system 200, since the moisture permeable membrane of the moisture permeable membrane device 24 is formed into a hollow fibril shape, the pressure of the air introduced into the moisture permeable membrane device 24 can be adjusted by the pressure adjusting device 30, and the moisture permeable can be adjusted. The humidity of the air derived by the membrane device 24 is particularly suitable for adjusting the humidity in the coating chamber to a humidity of about 30 to 70% (RH). As the pressure adjusting device 30, as long as the pressure can be accurately adjusted, for example, a diaphragm type can be used. As the pressure adjusting device 30, a person who can adjust the pressure in the range of 0.02 to 1.0 MPa can be used.

本實施形態相關之微針製劑製造用系統200 中的空氣過濾器16,只要是能夠捕捉通過空氣中所包含 的細菌、真菌類等微生物並除菌者即可,並無限制其使用。藉由使用如此之空氣過濾器16,不僅能夠去除微生物,亦能夠去除空氣中的塵埃。過濾器16之孔徑,以除菌效率之觀點來看,為0.2μm以下較佳。且,例如,能夠組合HEPA(High Efficiency Particulate Air)過濾器等具有除塵效果的過濾器、與具有除菌效果的空氣過濾器等,使用2個以上的空氣過濾器。本實施形態相關之系統200內,由於空氣壓縮機10所供給之空氣會不間斷地流向塗布腔室20之開口21,藉由於本系統200內具備空氣過濾器16,能夠更確實地將塗布腔室20內保持在無菌狀態。雖然空氣過濾器16是設置在風量調節裝置14的下游側,但能夠設置在從本系統200內之空氣壓縮機10到下游側之送風管線L上的任意位置。其中,由設置布局上及壓力控制之效率關係來看,設置在濕度調節裝置18之下游較佳。 The air filter 16 in the system for producing a microneedle preparation according to the present embodiment is not limited to any one as long as it can capture microorganisms such as bacteria and fungi contained in the air and is sterilized. By using such an air filter 16, it is possible to remove not only microorganisms but also dust in the air. The pore diameter of the filter 16 is preferably 0.2 μm or less from the viewpoint of sterilization efficiency. In addition, for example, a filter having a dust removing effect such as a HEPA (High Efficiency Particulate Air) filter or an air filter having a sterilization effect can be used, and two or more air filters can be used. In the system 200 according to the present embodiment, since the air supplied from the air compressor 10 flows uninterruptedly to the opening 21 of the coating chamber 20, the air filter 16 is provided in the system 200, so that the coating chamber can be more reliably The chamber 20 remains sterile. Although the air filter 16 is provided on the downstream side of the air volume adjusting device 14, it can be disposed at any position from the air compressor 10 in the present system 200 to the air supply line L on the downstream side. Among them, it is preferable to be disposed downstream of the humidity adjusting device 18 in view of the relationship between the arrangement layout and the pressure control efficiency.

本實施形態相關之微針製劑製造用系統200 中的送風管線L,無論其材質,只要是沒有空氣漏出即可,亦可使用任何形態。為了更確實壓縮空氣溫度調節裝置12所造成的溫度調節之效果,並更安定地將塗布腔室20內之空氣環境維持在所期望之溫度,送風管線L為具有阻熱效果者更佳。為了使送風管線L具有阻熱效果之方法,亦可將阻熱材料設置成包覆送風管線L之周圍的形態,亦可將送風管線L之材質本身作為具有阻熱效果之素材。 The microneedle preparation manufacturing system 200 according to the embodiment The air supply line L in the middle may be any form as long as it has no air leakage. In order to more reliably suppress the effect of the temperature adjustment caused by the air temperature adjusting device 12, and to more stably maintain the air environment in the coating chamber 20 at a desired temperature, the air supply line L is preferably a heat blocking effect. In order to make the air supply line L have a heat-blocking effect, the heat-insulating material may be disposed to cover the periphery of the air supply line L, or the material of the air supply line L may be used as a material having a heat-blocking effect.

由濕度調節裝置18以特定範圍內之溫濕度被 導出,且經空氣過濾器16除菌之空氣,在內部會被送至用於將包含藥劑之塗布液塗布於微針來製造微針製劑之塗布腔室20中。塗布腔室20中,在其壁面之一部分具有開口21。此開口21不僅作為排出由本系統200所供給之空氣的排氣口,亦具有塗布有塗布液之微針製劑的搬入口之角色。開口21,當塗布腔室20為例如箱型時,亦可設置在塗布腔室20的上面,亦可設置在側面或下面。為了使塗布腔室20內充分地滿足所期望之空氣環境,開口21與本系統200之連接部分充分地分離較佳。吹入塗布腔室20中的空氣之風量,充分保持在高量較佳。藉由將風量充分地保持在高量,能夠將塗布腔室20內保持在相對於本系統200之外部為正壓,並防止外部的空氣從開口21流入塗布腔室20內。因此,能夠將塗布腔室20內維持在所期望之溫濕度,且,能夠防止菌類從開口21侵入至塗布腔室20內部。 The humidity and humidity adjustment device 18 is temperature and humidity within a specific range. The air which is taken out and sterilized by the air filter 16 is internally sent to the coating chamber 20 for applying the coating liquid containing the drug to the microneedles to manufacture the microneedle preparation. The coating chamber 20 has an opening 21 at a portion of its wall surface. This opening 21 functions not only as an exhaust port for discharging the air supplied from the system 200 but also as a carry-in port for the microneedle preparation to which the coating liquid is applied. The opening 21, when the coating chamber 20 is, for example, a box type, may be disposed on the upper surface of the coating chamber 20 or on the side or below. In order to adequately satisfy the desired air environment within the coating chamber 20, it is preferred that the opening 21 is sufficiently separated from the portion of the system 200. The amount of air blown into the coating chamber 20 is preferably maintained at a high amount. By sufficiently maintaining the air volume at a high amount, the inside of the coating chamber 20 can be maintained at a positive pressure with respect to the outside of the system 200, and external air can be prevented from flowing into the coating chamber 20 from the opening 21. Therefore, it is possible to maintain the inside of the coating chamber 20 at a desired temperature and humidity, and it is possible to prevent the fungus from entering the inside of the coating chamber 20 from the opening 21.

塗布腔室20之內部中,為了把握塗布腔室20 內的空氣之溫濕度,設置溫濕度探測器(溫度探測器及濕度探測器)26較佳。是因為由於能夠隨時把握由本系統200供給至塗布腔室20內的空氣是否維持在所期望之溫濕度,故能夠因應塗布腔室20內之溫濕度,依序操作壓力調節裝置30、壓縮空氣溫度調節裝置12及濕度調節裝置18,更進而嚴格地控制塗布腔室20內之空氣的溫濕度。且,亦可設置一系統,將對應於溫濕度探測器26所 檢測出的塗布腔室20內之溫度及濕度的信號送入控制裝置(控制壓力調節裝置30之第1控制手段及/或第2控制手段、控制壓縮空氣溫度調節裝置12之第3控制手段及/或第4控制手段、以及控制水分供給器22之水溫之第5控制手段及/或第6控制手段)28,基於其信號,控制裝置28會操作壓力調節裝置30、壓縮空氣溫度調節裝置12或濕度調節裝置18內之水分供給器22之系統,亦即回饋系統。具體來說,能夠設置例如一種回饋系統,其係若檢測到塗布腔室20內之濕度低下,則會使壓力調節裝置30之設定壓力有下降動作,相反地若檢測到塗布腔室20內之濕度上升,則使壓力調節裝置30之設定壓力有上升動作。同樣地,能夠設置例如一種回饋系統,其係檢測到塗布腔室20內之濕度低下後,則使水分供給器22之加熱機構動作,相反地若檢測到塗布腔室20內之濕度上昇後,則使水分供給器22之冷卻機構動作。且,能夠設置例如,若檢測到塗布腔室20內之溫度比特定之下限值更低,則促進壓縮空氣溫度調節裝置12之加熱機構之加熱,或抑制冷卻機構之冷卻,相反地,若檢測到塗布腔室20內之溫度比特定之上限值更高,則抑制壓縮空氣溫度調節裝置12之加熱機構之加熱,或促進冷卻機構之冷卻之回饋系統。藉由設置如此之回饋系統,能夠更有效率且確實地進行塗布腔室20內之溫濕度控制。 In the interior of the coating chamber 20, in order to grasp the coating chamber 20 The temperature and humidity of the air inside is preferably set to a temperature and humidity detector (temperature detector and humidity detector) 26. This is because it is possible to constantly control whether the air supplied from the system 200 into the coating chamber 20 is maintained at a desired temperature and humidity, so that the pressure adjusting device 30 and the compressed air temperature can be sequentially operated in accordance with the temperature and humidity in the coating chamber 20. The adjusting device 12 and the humidity adjusting device 18 further strictly control the temperature and humidity of the air in the coating chamber 20. Moreover, a system can also be provided, which will correspond to the temperature and humidity detector 26 The detected temperature and humidity signal in the coating chamber 20 is sent to the control device (the first control means for controlling the pressure adjusting device 30 and/or the second control means, and the third control means for controlling the compressed air temperature adjusting means 12 and / or the fourth control means and the fifth control means and/or the sixth control means 28 for controlling the water temperature of the water supplier 22, based on the signal, the control means 28 operates the pressure adjusting means 30 and the compressed air temperature adjusting means 12 or a system of moisture supply 22 in humidity conditioning device 18, that is, a feedback system. Specifically, for example, a feedback system can be provided which detects that the set pressure of the pressure adjusting device 30 is lowered if the humidity in the coating chamber 20 is lowered, and conversely, if the coating chamber 20 is detected. When the humidity rises, the set pressure of the pressure adjusting device 30 is raised. Similarly, for example, a feedback system can be provided which detects the heating mechanism of the moisture supplier 22 after detecting that the humidity in the coating chamber 20 is low, and conversely, if the humidity in the coating chamber 20 is detected to rise, Then, the cooling mechanism of the moisture supplier 22 is operated. Further, for example, if it is detected that the temperature in the coating chamber 20 is lower than a specific lower limit value, the heating of the heating mechanism of the compressed air temperature adjusting device 12 is promoted, or the cooling of the cooling mechanism is suppressed, and conversely, When it is detected that the temperature in the coating chamber 20 is higher than a certain upper limit, the heating of the heating mechanism of the compressed air temperature adjusting device 12 is suppressed, or the cooling feedback system of the cooling mechanism is promoted. By providing such a feedback system, temperature and humidity control within the coating chamber 20 can be performed more efficiently and reliably.

若使如以上之構成的微針製劑製造用系統200動作,則首先,空氣會經空氣壓縮機10而從外部被吸 入,並供給至本系統200內。被空氣壓縮機10供給的空氣,會通過送風管線L而注入壓縮空氣溫度調節裝置12中,並被調節成特定之溫度。經壓縮空氣溫度調節裝置12而調節成特定溫度之空氣,會通過送風管線L,注入壓力調節裝置30中,並被調節成特定之壓力。壓力經壓力調節裝置30調節的空氣會通過送風管線L,並注入濕度調節裝置18中,被調節成特定之濕度。濕度經濕度調節裝置18調節的空氣,因應必要在風量調節後,會經空氣過濾器16除菌。如此溫濕度經調節且無菌狀態之空氣會通過送風管線L,而供給至塗布腔室20內。先前存在於塗布腔室20內的空氣,會從設置於構成塗布腔室20之壁面的一部分上的開口21被排出,塗布腔室20之內部會充滿具有所期望之溫濕度且為無菌狀態之空氣。從開口21會隨時排出以本系統200而供給至塗布腔室20內的空氣。流通於本系統200內的空氣,會因為空氣壓縮機10的送風力,而時常以具有某個程度的風速之狀態,朝向開口21以同一方向流動。因此,空氣不會滯留在本系統200的內部,且即使在本系統200內部有細菌存在,其繁殖也會被抑制。 When the microneedle preparation manufacturing system 200 having the above configuration is operated, first, air is sucked from the outside through the air compressor 10. Into, and supplied to the system 200. The air supplied by the air compressor 10 is injected into the compressed air temperature adjusting device 12 through the air supply line L, and is adjusted to a specific temperature. The air adjusted to a specific temperature by the compressed air temperature adjusting device 12 is injected into the pressure adjusting device 30 through the air supply line L, and is adjusted to a specific pressure. The air whose pressure is regulated by the pressure adjusting device 30 passes through the air supply line L and is injected into the humidity adjusting device 18 to be adjusted to a specific humidity. The air whose humidity is adjusted by the humidity adjusting device 18 is sterilized by the air filter 16 after the air volume adjustment is necessary. The air whose temperature and humidity are adjusted and sterilized is supplied to the coating chamber 20 through the air supply line L. The air previously present in the coating chamber 20 is discharged from the opening 21 provided in a portion of the wall surface constituting the coating chamber 20, and the inside of the coating chamber 20 is filled with the desired temperature and humidity and is sterilized. air. The air supplied to the coating chamber 20 by the present system 200 is discharged from the opening 21 at any time. The air that has flowed through the system 200 flows in the same direction toward the opening 21 in a state of having a certain degree of wind speed due to the wind power supplied from the air compressor 10. Therefore, air does not remain inside the system 200, and even if bacteria are present inside the system 200, the reproduction is suppressed.

塗布腔室20內中,可事先準備塗布於微針之 包含藥劑之塗布液。塗布作業的期間,如前述所示,由於塗布腔室20內時常為特定範圍之溫濕度且為無菌狀態之環境下,故塗布液中所含有的水之氣化反應、及空氣中之水分的液化反應會受到控制,並能抑制塗布液物性的變 化。因此,能夠抑制塗布於微針上之藥劑量的不均勻,並能在無菌環境下安定地生產微針製劑。表示塗布於微針上之藥劑量之不均勻的左右之CV(變動係數)值為10%以下較佳,為5%以下更佳。CV值意指將標準偏差除以平均值,並以百分率來表示之值。 In the coating chamber 20, it can be prepared to be applied to the microneedles in advance. A coating solution containing a drug. During the coating operation, as described above, since the coating chamber 20 is often in a specific range of temperature and humidity and in an aseptic environment, the gasification reaction of water contained in the coating liquid and the moisture in the air are caused. The liquefaction reaction is controlled and can inhibit the change of the physical properties of the coating liquid. Chemical. Therefore, unevenness in the amount of the drug applied to the microneedles can be suppressed, and the microneedle preparation can be stably produced in a sterile environment. The CV (coefficient of variation) value of the left and right sides of the amount of the drug applied to the microneedles is preferably 10% or less, more preferably 5% or less. The CV value means the value obtained by dividing the standard deviation by the average value and expressed as a percentage.

雖然來自空氣壓縮機10之空氣的風量(流 量)能夠藉由空氣壓縮機10本身的機能來調節,但藉由於空氣壓縮機10之下游側連接風量調節裝置14,能夠來高精密度地調節流通於本系統200內之空氣的風量較佳。 本系統200包含風量調節裝置14時,藉由些微調整流通於本系統200內之空氣的風量,能夠控制塗布於微針上的藥劑量。且,風量為一定量以上時,例如為0.5L/min以上後,則能夠更均勻化塗布腔室內中的溫濕度分布。風量調節裝置14以設置布局上及壓力控制之效率之觀點來看,設置在濕度調節裝置18的下游較佳。 Although the amount of air from the air compressor 10 (flow) The amount can be adjusted by the function of the air compressor 10 itself. However, since the air volume adjusting device 14 is connected to the downstream side of the air compressor 10, it is possible to adjust the air volume of the air flowing through the system 200 with high precision. . When the system 200 includes the air volume adjusting device 14, the amount of the air applied to the microneedles can be controlled by slightly adjusting the amount of air flowing through the system 200. Further, when the air volume is a certain amount or more, for example, 0.5 L/min or more, the temperature and humidity distribution in the coating chamber can be more uniformized. The air volume adjusting device 14 is preferably disposed downstream of the humidity adjusting device 18 from the viewpoint of setting the layout and the efficiency of the pressure control.

上述實施形態中,設置本系統200的環境之 溫度雖然以會變動者來說明,但在環境全體之溫度被控制的空間中,使用本系統200時等,由空氣壓縮機10所供給之空氣已經被保持在特定範圍之溫度時,在構成當中亦可不用具備壓縮空氣溫度調節裝置12。 In the above embodiment, the environment of the system 200 is set. Although the temperature is described as a changer, when the system 200 is used in a space where the temperature of the entire environment is controlled, when the air supplied from the air compressor 10 has been maintained at a specific temperature, it is in the middle of construction. It is also possible not to have the compressed air temperature adjustment device 12.

且,濕度調節裝置18,雖然以具有含有中空 纖絲狀之透濕膜的透濕膜裝置24者來說明,但透濕膜並不限定於中空纖絲狀之形狀,亦可使用任意形狀者。圖3所示之濕度調節裝置18,具有設置在隔壁型上的透濕膜 23。圖3中的透濕膜23會將由空氣壓縮機10而供給至本系統200內的空氣、與作為濕度調節源的水分分離。水分會介隔著透濕膜23,並作為水蒸氣供給至流通於本系統200之流路內的空氣中。 Moreover, the humidity adjusting device 18 has a hollow The moisture permeable membrane device 24 of the fibril-like moisture permeable membrane is described, but the moisture permeable membrane is not limited to the hollow filament shape, and any shape may be used. The humidity adjusting device 18 shown in Fig. 3 has a moisture permeable film disposed on the partition type twenty three. The moisture permeable film 23 in Fig. 3 separates the air supplied to the system 200 by the air compressor 10 from the moisture as a humidity control source. The moisture permeates the moisture permeable membrane 23 and is supplied as water vapor to the air flowing through the flow path of the system 200.

圖3中之壓力調節裝置30,會連接在濕度調 節裝置18之上游側的外部,並調節導入濕度調節裝置18內之空氣的壓力。且,亦可將壓力調節裝置30設置於濕度調節裝置18之內部,並調節導入濕度調節裝置18內的空氣之壓力。 The pressure regulating device 30 in Fig. 3 is connected to the humidity adjustment The outside of the upstream side of the device 18 adjusts the pressure of the air introduced into the humidity control device 18. Further, the pressure adjusting device 30 may be disposed inside the humidity adjusting device 18 and adjust the pressure of the air introduced into the humidity adjusting device 18.

使用以上構成中的微針製劑製造用系統,針 對製造微針製劑方法,說明概要。圖4為表示使用本實施形態相關之系統所製造之微針製劑之一例的斜視圖。如圖4所示之微針製劑40具備基板42、與以二次元狀配置於基板42上之複數微針44、與形成於微針44上之塗布層46。塗布層46為使用本實施形態相關之微針製劑製造用系統所塗布者,其揮發成分的至少一部份被去除較佳。 Using the system for manufacturing a microneedle preparation in the above configuration, the needle An outline of the method for producing a microneedle preparation is described. Fig. 4 is a perspective view showing an example of a microneedle preparation produced by using the system according to the embodiment. The microneedle preparation 40 shown in FIG. 4 includes a substrate 42 and a plurality of microneedles 44 disposed on the substrate 42 in a bipolar shape, and a coating layer 46 formed on the microneedles 44. The coating layer 46 is applied by using the system for producing a microneedle preparation according to the present embodiment, and at least a part of the volatile component is preferably removed.

基板42是用於支持微針44的基台。基板42 之面積為0.5~10cm2較佳,更佳為1~5cm2,再更佳為1~3cm2。亦可藉由結合數個此基板42,來構成所期望之大小的基板。 The substrate 42 is a base for supporting the microneedles 44. The area of the substrate 42 is preferably 0.5 to 10 cm 2 , more preferably 1 to 5 cm 2 , still more preferably 1 to 3 cm 2 . A substrate of a desired size can also be formed by combining a plurality of the substrates 42.

微針44為微小構造,其高度(長度)較佳為 50~600μm。於此,藉由將微針44之長度設在50μm以上,能夠確實地進行塗布液中所包含之藥劑的投予。且,藉由將微針44之長度設在600μm以下,可以迴避微針 接觸到神經,並確實地減少疼痛的可能性,並同時回避出血的可能性。且,微針44的長度為500μm以下的話,能夠效率良好地投予應進入皮內之量的藥劑,且不使基底膜穿孔即能夠投予。微針44之長度為300~500μm特別佳。 The microneedles 44 have a minute structure and have a height (length) of preferably 50 to 600 μm. Here, by setting the length of the microneedles 44 to 50 μm or more, the administration of the drug contained in the coating liquid can be reliably performed. Moreover, by setting the length of the microneedles 44 to 600 μm or less, it is possible to avoid contact of the microneedles with the nerves, and to surely reduce the possibility of pain while avoiding the possibility of bleeding. Further, when the length of the microneedles 44 is 500 μm or less, the amount of the drug to be injected into the skin can be efficiently administered, and the base film can be administered without being perforated. The length of the microneedles 44 is particularly preferably 300 to 500 μm.

於此,微針44意指凸狀構造物,且廣泛意味 著針形狀、或包含針形狀之構造物。不過,微針並非限定於具有尖銳前端之針形狀者,亦可為前端非尖銳的形狀。 微針44為圓錐狀構造時,其基底的直徑為50~200μm左右較佳。本實施形態中,微針44雖為圓錐狀,但亦可為四角錐等多角錐狀、或其他形狀之微針。 Here, the microneedle 44 means a convex structure, and broadly means a needle shape or a structure including a needle shape. However, the microneedle is not limited to a needle shape having a sharp front end, and may have a non-sharp shape at the front end. When the microneedle 44 has a conical structure, the diameter of the base is preferably about 50 to 200 μm . In the present embodiment, the microneedles 44 have a conical shape, but may be a polygonal pyramid such as a quadrangular pyramid or a microneedle of another shape.

微針44,典型來說設置成為,在針的橫列, 以每1公釐(mm)為約1~10根的密度之間隔來分開。一般來說,鄰接的橫列,相對於橫列內之針的空間,實質上僅互相以相等之距離分離,並具有在每1cm2中為100~10000根之針密度。若具有100根以上的針密度,能夠效率良好地穿過皮膚。另一方面,超過10000根的針密度,較難保持微針44的強度。微針44之密度較佳為200~5000根,更佳為300~2000根,特別佳為400~850根。 The microneedles 44 are typically arranged to be separated at intervals of a density of about 1 to 10 per 1 mm in the course of the needle. In general, the adjacent courses are substantially separated from each other by an equal distance with respect to the space of the needles in the course, and have a needle density of 100 to 10,000 per 1 cm 2 . If it has a needle density of 100 or more, it can pass through the skin efficiently. On the other hand, with a needle density of more than 10,000, it is difficult to maintain the strength of the microneedles 44. The density of the microneedles 44 is preferably 200 to 5,000, more preferably 300 to 2,000, and particularly preferably 400 to 850.

作為基板42或微針44之材質,雖有舉出 矽、二氧化矽、瓷器、金屬(不鏽鋼、鈦、鎳、鉬、鉻、鈷等)及合成或天然樹脂素材等,但考慮微針之抗原性及材質的單價,則以聚乳酸、聚乙交酯、聚乳酸-co-聚乙交 酯、支鏈澱粉、己內酯、聚氨酯、聚酐等生物分解性聚合物、或非分解性聚合物的聚碳酸酯、聚甲基丙烯酸、乙烯乙酸乙烯、聚四氟乙烯、聚縮醛等合成或天然樹脂素材特別佳。且,多糖類的玻尿酸、玻糖醛酸鈉、支鏈澱粉、六碳醣、糊精或硫酸軟骨素等亦適合。 As the material of the substrate 42 or the microneedles 44, although Antimony, cerium oxide, porcelain, metal (stainless steel, titanium, nickel, molybdenum, chromium, cobalt, etc.) and synthetic or natural resin materials, etc., but considering the antigenicity of the microneedles and the unit price of the material, polylactic acid, polyethylene Lactide, polylactic acid-co-polyethylene Biodegradable polymer such as ester, amylopectin, caprolactone, polyurethane, polyanhydride or polycarbonate of non-decomposable polymer, polymethacrylic acid, ethylene vinyl acetate, polytetrafluoroethylene, polyacetal, etc. Synthetic or natural resin materials are especially good. Further, hyaluronic acid, sodium hyaluronate, amylopectin, hexose, dextrin or chondroitin sulfate are also suitable.

作為基板42或微針44之製法,有舉出使用 矽基板之濕式蝕刻加工或乾性蝕刻加工、使用金屬或樹脂之精密機械加工(放電加工、雷射加工、切割加工、熱壓成型加工、射出成型加工等)、機械切削加工等。藉由此等之加工法,基板42與微針44被成型為一體。作為將微針44成為中空之方法,有舉出在製作微針44後,以雷射等進行2次加工之方法。 As a method of manufacturing the substrate 42 or the microneedle 44, there is a use Wet etching or dry etching of a substrate, precision machining using metal or resin (electric discharge machining, laser machining, cutting, hot press molding, injection molding, etc.), mechanical cutting, and the like. The substrate 42 and the microneedles 44 are integrally molded by this processing method. As a method of making the microneedles 44 hollow, there is a method of performing the secondary processing by laser or the like after the microneedles 44 are produced.

微針製劑40中,在微針44上雖然具備塗布 層46,但塗布層46藉由塗布塗布液來形成較佳。作為塗布方法,有舉出噴霧塗覆及浸漬塗覆等,以浸漬塗覆較佳。且,圖4中,雖然在全部的微針44上都形成有塗布層46,但塗布層46僅形成於複數存在之微針44中的一部分即可。且圖4中,雖然塗布層46僅形成於微針44的前端部分,但亦可形成為包覆於微針44之全體。進而,塗布層46亦可形成於基板42上。 In the microneedle preparation 40, although the microneedle 44 is coated Layer 46, but coating layer 46 is preferably formed by coating a coating liquid. As the coating method, spray coating, dip coating, or the like is exemplified, and dip coating is preferred. Further, in FIG. 4, the coating layer 46 is formed on all of the microneedles 44, but the coating layer 46 may be formed only in a part of the plurality of microneedles 44 present. In FIG. 4, although the coating layer 46 is formed only at the front end portion of the microneedles 44, it may be formed so as to be coated on the entire microneedles 44. Further, the coating layer 46 may be formed on the substrate 42.

圖5為圖4之V-V線剖面圖。如圖5所示, 微針製劑40為具備基板42、與設置在基板42上的微針44、與設置於該微針44上的塗布層46者。附著於微針上的塗布層46為含有藥劑者,例如能夠經上述步驟來製 造。 Figure 5 is a cross-sectional view taken along line V-V of Figure 4; As shown in Figure 5, The microneedle preparation 40 is provided with a substrate 42, a microneedle 44 provided on the substrate 42, and a coating layer 46 provided on the microneedle 44. The coating layer 46 attached to the microneedles is a drug-containing one, and can be produced, for example, by the above steps. Made.

圖6(a)、(b)及(c)為表示微針製劑40 之製造方法的一示例之圖。此方法稱為浸漬方式。在此方法中,首先,如圖6(a)所示,在屏障板52上將塗布液50以刮勺54往箭頭A的方向刮過。藉此,於開口部56中填充塗布液50。接著,如圖6(b)所示,將微針44插入屏障板52之開口部56。之後,如圖6(c)所示,將微針44從屏障板52之開口部56拔出。藉此,使塗布液50附著於微針44上。且,亦可使塗布液50附著於基板42上。 Figures 6(a), (b) and (c) show the microneedle preparation 40 An example of a manufacturing method. This method is called the dipping method. In this method, first, as shown in FIG. 6(a), the coating liquid 50 is scraped on the barrier sheet 52 in the direction of the arrow A by the spatula 54. Thereby, the coating liquid 50 is filled in the opening 56. Next, as shown in FIG. 6(b), the microneedles 44 are inserted into the opening portion 56 of the barrier panel 52. Thereafter, as shown in FIG. 6(c), the microneedles 44 are pulled out from the opening 56 of the barrier panel 52. Thereby, the coating liquid 50 is attached to the microneedles 44. Further, the coating liquid 50 may be attached to the substrate 42.

雖然是藉由在塗布腔室內進行圖6(a)、 (b)及(c)所示之作業,來製造微針製劑,但作為此時之條件,藉由使用本實施形態相關之系統,來將塗布腔室內成為溫濕度經控制之無菌狀態的空氣環境。具體來說是,啟動本系統中的各裝置,並將由空氣壓縮機所供給之空氣調節成為所期望之環境,再吹入塗布腔室內。藉由將塗布腔室內之溫濕度計測結果回饋於恆溫水槽等,能夠安定地維持在所期望之溫濕度的空氣環境。藉由在如此所得之空氣環境下進行塗布,能夠於微針上安定地塗布一定藥劑含量之塗布液。 Although it is carried out in the coating chamber by Fig. 6(a), (b) and (c), the microneedle preparation is manufactured, but as a condition at this time, the coating chamber is made into a sterilized air having a controlled temperature and humidity by using the system according to the embodiment. surroundings. Specifically, each device in the system is activated, and the air supplied by the air compressor is adjusted to a desired environment and then blown into the coating chamber. By returning the temperature and humidity measurement result in the coating chamber to the constant temperature water tank or the like, it is possible to stably maintain the air environment of the desired temperature and humidity. By coating in the air atmosphere thus obtained, it is possible to stably apply a coating liquid having a certain chemical content to the microneedles.

如上述進行塗布後,藉由風乾、真空乾燥、 或此等之組合之習知的方法,來去除微針44上之塗布液50的揮發成分。藉此,塗布層46會堅固地附著在微針44上,並成為典型的玻璃質或固體狀,來製造微針製劑 40。塗布層46之水分含有量通常以塗布層46之全量基準下,為55質量%以下,更佳為30質量%以下,進一步為10質量%以下。藉由上述方法,能夠防止所附著之塗布液50的液體滴落。液體滴落意指,塗布液從針頭滴下之意,在圖6(c)中意指H部分變長。 After coating as described above, by air drying, vacuum drying, Or a combination of these, a method of removing the volatile component of the coating liquid 50 on the microneedles 44. Thereby, the coating layer 46 is firmly adhered to the microneedles 44 and becomes a typical vitreous or solid to manufacture a microneedle preparation. 40. The water content of the coating layer 46 is usually 55 mass% or less, more preferably 30 mass% or less, and further 10 mass% or less, based on the total amount of the coating layer 46. According to the above method, it is possible to prevent the liquid of the applied coating liquid 50 from dripping. The liquid dripping means that the coating liquid is dripped from the needle, and in Fig. 6(c), the H portion is elongated.

附著於微針44上的塗布層46之高度H,以如圖6(b)所示之間隙(縫隙)C來作調整。此間隙C定義為,從微針44之基底至屏障板52表面的距離(與基板42的厚度無關),並因應屏障板52之拉力與微針44之長度來設定。間隙C之距離的範圍較佳為0~500μm。間隙C之距離為0時,意指塗布液50被塗覆於微針44之全體。附著於微針44上之塗布液50的高度H會因為微針44的高度而變動,但能夠為0~500μm,通常為10~500μm,較佳為30~300μm左右,特別佳為40~250μm左右。為了有效地使用塗布液50中的藥劑,集中存在微針的一部分,亦即針的前端部分較佳,且,對皮膚之刺激及藥物對皮膚之移行率的觀點來看,也是存在於前端至200μm較佳。塗布液50,能夠例如將高分子化合物溶解於水溶液中,且具有高黏度來說,能夠在微針之一部分形成塗布層46。以如此之形態保持在微針44上的塗布液50,會在微針44穿刺於皮膚時,同時插入皮內。 The height H of the coating layer 46 attached to the microneedles 44 is adjusted by a gap (slit) C as shown in Fig. 6(b). This gap C is defined as the distance from the base of the microneedle 44 to the surface of the barrier plate 52 (independent of the thickness of the substrate 42) and is set in accordance with the tensile force of the barrier plate 52 and the length of the microneedle 44. The distance of the gap C is preferably in the range of 0 to 500 μm . When the distance of the gap C is 0, it means that the coating liquid 50 is applied to the entirety of the microneedles 44. The height H of the coating liquid 50 adhering to the microneedles 44 varies depending on the height of the microneedles 44, but can be 0 to 500 μm , usually 10 to 500 μm , preferably about 30 to 300 μm . Especially good is about 40~250 μm . In order to effectively use the agent in the coating liquid 50, a part of the microneedle is concentrated, that is, the tip end portion of the needle is preferable, and from the viewpoint of skin irritation and drug migration rate to the skin, it is also present at the front end to 200 μ m is preferred. The coating liquid 50 can dissolve the polymer compound in an aqueous solution, for example, and can form the coating layer 46 in one of the microneedles with high viscosity. The coating liquid 50 held on the microneedles 44 in such a manner is simultaneously inserted into the skin while the microneedles 44 are punctured to the skin.

附著於微針44上的塗布層46在乾燥後的厚度為未滿50μm較佳,更佳為未滿40μm,再更佳為1~30μm。一般來說,附著於微針上之塗布層46的厚 度,在乾燥後跨過微針44之表面所測定的平均厚度。附著於微針44上的塗布層46之厚度,會因為適用於塗布液50之複數被膜而增加,亦即,在使塗布液50附著後,能夠藉由重複附著步驟而使其增加。 The coating layer 46 adhered to the microneedles 44 preferably has a thickness of less than 50 μm after drying, more preferably less than 40 μm , still more preferably 1 to 30 μm . Generally, the thickness of the coating layer 46 attached to the microneedles is the average thickness measured across the surface of the microneedles 44 after drying. The thickness of the coating layer 46 adhering to the microneedles 44 is increased by the plurality of coatings applied to the coating liquid 50, that is, after the coating liquid 50 is attached, it can be increased by repeating the adhesion step.

作為塗布液50中所含之藥劑,認為例如有胜 肽、蛋白質、DNA、RNA等高分子化合物,但無特別限定,只要分子量為1000左右,即亦可為疫苗、低分子胜肽、糖、核酸等。作為生理活性物質,有舉例如納曲酮、乙酸西曲瑞克、他替瑞林、那法瑞林乙酸鹽、前列腺素A1、亞普列腺素、α-干擾素、用於多發性硬化症之β-干擾素、紅血球生成素、促濾泡素β、促濾泡素α、G-CSF、GM-CSF、人類絨毛性腺刺激賀爾蒙、黃體形成(leutinizing)賀爾蒙、鮭降鈣素、升糖素、GNRH抗拮劑、胰島素、人類成長賀爾蒙、惠爾血添、肝素、低分子肝素、生長激素、腸促胰島素、GLP-1誘導體等。且,作為疫苗類之示例,有舉出日本腦炎疫苗、輪狀病毒疫苗、老年癡呆症疫苗、動脈硬化疫苗、癌疫苗、尼古丁疫苗、白喉症疫苗、破傷風疫苗、百日咳疫苗、萊姆病疫苗、狂犬病疫苗、肺炎雙球菌疫苗、黃熱病疫苗、霍亂疫苗、牛痘疫苗、結核疫苗、德國麻疹疫苗、麻疹疫苗、腮腺炎疫苗、肉毒桿菌疫苗、皰疹病毒疫苗、其他DNA疫苗、B型肝炎疫苗等。 As the agent contained in the coating liquid 50, for example, there is a victory. The polymer compound such as a peptide, a protein, a DNA, or an RNA is not particularly limited, and may have a molecular weight of about 1,000, that is, a vaccine, a low molecular peptide, a sugar, or a nucleic acid. As physiologically active substances, for example, naltrexone, cetrorelix acetate, statin, nafarelin acetate, prostaglandin A1, apredrainin, α-interferon, for multiple sclerosis Β-interferon, erythropoietin, follicle stimulating hormone β, follicle stimulating α, G-CSF, GM-CSF, human villus gonad stimulation hormone, leuntizing hormone, sputum Calcitonin, glycoside, GNRH anti-antagonism, insulin, human growth hormone, Whirlpool blood, heparin, low molecular weight heparin, growth hormone, incretin, GLP-1 inducer, and the like. Further, examples of vaccines include Japanese encephalitis vaccine, rotavirus vaccine, Alzheimer's disease vaccine, arteriosclerosis vaccine, cancer vaccine, nicotine vaccine, diphtheria vaccine, tetanus vaccine, pertussis vaccine, and Lyme disease vaccine. , rabies vaccine, pneumococcal vaccine, yellow fever vaccine, cholera vaccine, vaccinia vaccine, tuberculosis vaccine, German measles vaccine, measles vaccine, mumps vaccine, botulinum vaccine, herpes virus vaccine, other DNA vaccine, hepatitis B Vaccines, etc.

其他,有舉例如,催眠.鎮靜劑(鹽酸氟路 洛,鹽酸利馬扎封,苯巴比妥,異戊巴比妥等),解熱消 炎鎮痛劑(酒石酸布托啡諾,檸檬酸吡哆醛,乙醯氨酚,邁菲那密酸,二克氯吩鈉,阿司匹林,阿氯芬酸,可多普洛菲,氟白普洛芬,那普洛辛,匹洛卡,鎮痛新,引朵甲阿辛,水楊酸二醇,匹拉米酮,洛索洛芬等),類固醇系抗炎症劑(皮質醇,去氫皮質醇,地塞米松,貝皮質醇等),興奮.刺激劑(鹽酸甲基安非他明,鹽酸哌甲酯等),精神神經用劑(鹽酸伊米胺,二氮平,鹽酸樂復得,縮蘋酸氟伍洒胺,鹽酸帕羅西汀,溴化氫西酞普蘭,鹽酸百憂解,三氮二氮平,多巴胺拮抗劑,可洛米普明,阿米曲替林,地昔帕明,安莫散平,馬普替林,米塞林,司普替林,妥解鬱錠,洛非帕明,米那普侖,杜洛西汀,速悅,鹽酸酚塞素,甲硫達嗪,二氮平,美普巴邁,依替唑侖等),賀爾蒙劑(動情素,雌三醇,助孕素,乙酸降雄甾炔酮,乙酸美替諾龍,睪丸固酮等),局部麻醉劑(鹽酸利多卡因,鹽酸奴佛卡因,鹽酸四卡因,鹽酸待布卡因,鹽酸丙胺卡因等),泌尿器官用劑(鹽酸達多幫,鹽酸坦洛新,鹽酸丙哌維林等),骨格筋弛緩劑(鹽酸替扎尼定,鹽酸乙哌立松,甲磺酸哌二苯丙醇,鹽酸琥珀膽鹼,等),生殖器官用劑(鹽酸利托君,酒石酸美聲君),抗癲癇劑(二丙基醋酸鈉,可羅平,卡巴氮平等),自律神經用劑(氯化三甲胺丁酸甲酯,溴化新斯狄明,氯化脂膽等),抗帕金森氏症劑(甲磺酸帕格萊,甲磺酸溴麥角克普汀,鹽酸顫立靜,鹽酸金剛胺,鹽酸力必平,鹽酸他利克索,過乳降錠,屈昔多巴,比培力汀,鹽 酸迪普寧等),利尿劑(氫氟甲苯噻,弗西邁等),呼吸促進劑(鹽酸山梗菜鹼,雙嗎啉胺,鹽酸拿咯松等),抗片頭痛劑(甲磺雙氫麥角胺,司麥普坦,酒石酸麥角胺,鹽酸氟苯桂淨,鹽酸塞浦西他啶等),抗組織胺劑(延胡索酸可利汀,鞣酸苯海拉明,縮蘋酸氯菲安明、鹽酸二苯吡拉林,鹽酸異丙嗪等),氣管支擴張劑(鹽酸妥布特羅,鹽酸克伏喘,硫酸沙丁胺醇,鹽酸克倫特羅,溴化氫酚丙喘寧,硫酸特布他林,硫酸異丙腎上腺素,富馬酸福莫特羅等),強心劑(鹽酸異丙腎上腺素,鹽酸多巴胺等),冠狀血管擴張劑(鹽酸迪太贊,鹽酸維拉帕米,硝酸冠欣錠,三硝酸甘油,尼可地爾等),末梢血管擴張劑(暢力糖衣錠,鹽酸苄咪唑啉等),禁煙補助藥(尼古丁等),循環器官用劑(鹽酸氟苯桂淨,鹽酸培爾吉平,尼川待平,尼索地平,菲洛的平,苯磺酸胺氯迪品,尼非待平,尼伐地平,鹽酸曼尼待平,鹽酸貝尼地平,縮蘋酸伊那拉普利,鹽酸替莫普利,阿拉普利,鹽酸咪達普利,西拉普利,利欣諾普,卡托普利,群多普利,叔丁胺培林普利,阿廷諾,反丁烯二酸必舒普洛,酒石酸美多心安,鹽酸倍他洛爾,鹽酸阿羅洛爾,鹽酸塞利洛爾,卡利索普若多錠,鹽酸卡替洛爾,鹽酸貝凡洛爾,纈沙坦,坎地沙坦片,洛沙坦鉀,鹽酸克尼丁等),心律不整用劑(鹽酸心得安,鹽酸心得舒,鹽酸奴佛卡因醯胺,鹽酸墨西律定,那杜洛,心達寧等),抗惡性潰瘍劑(環磷醯胺,氟尿嘧啶,友復膠囊,鹽酸普魯苄肼,雷莫司汀,鹽酸愛萊諾迪 肯,Fururijin等),抗脂血症劑(普伐他丁,辛伐他丁,本那非泊,剖巴可等),血糖降下劑(格力本,氯磺丙脲,甲苯磺丁脲,格列嘧啶鈉,格列丁唑,鹽酸丁二胍),消化性潰瘍治療劑(丙谷胺,鹽酸西曲酸酯,螺佐呋酮,甲氰咪胍,溴化葡萄糖吡喀),利膽劑(去氧熊膽酸,柳胺酚等),消化管運動改善劑(多普利杜,希塞菩等),肝臓疾患用劑(硫普羅寧等),抗過敏劑(富馬酸酮替芬,鹽酸氮卓斯丁等),抗病毒劑(阿昔洛韋等),鎮暈劑(敏使朗錠,鹽酸地芬尼多等),抗生劑(頭孢利定,頭孢地尼,頭孢泊肟酯,頭孢可若,克拉黴素,紅絲菌素,甲基紅絲菌素,硫酸卡那徽素,環絲氨酸,四環素,苄青黴素鉀,普匹西林,氯噻青黴素鈉,胺苄青黴素膠囊,鹽酸氨苄青黴素甲戊酯,卡茚西林鈉,氯黴素,等),習慣性中毒用劑(氰化銨等),食慾抑制劑(氯苯咪吲哚等),化學療法劑(異菸酸酊,乙硫異菸醯胺,吡井醯胺等),血液凝固促進劑(鹽酸噻氯匹啶,苄丙酮香豆素鉀),抗老年癡呆劑(毒扁豆鹼,鹽酸愛憶欣,塔克林,檳榔素,占諾美林等),血清素受容體拮抗止吐劑(鹽酸恩丹西酮,鹽酸康您適強,鹽酸雷莫司瓊,鹽酸鹽酸阿扎司瓊等),痛風治療劑(秋水仙素,二丙磺胺苯甲酸,亞磺吡唑等),麻藥系之鎮痛劑(檸檬酸吩坦尼,硫酸嗎啡,鹽酸嗎啡,磷酸可待因,鹽酸可卡因,鹽酸配西汀等)。 Others, such as hypnosis. Sedative Luo, limazabine hydrochloride, phenobarbital, isobarbital, etc.) Inflammatory analgesic (butorphanol tartrate, pyridoxal citrate, acetaminophen, mefenamic acid, sodium diclofenac, aspirin, aclofenac, docopyrene, flupeptone Fen, Naproxine, Piloca, New Analgesic, Acacia, Salicylic Acid Glycol, Pelidine, Loxoprofen, etc.), Steroid Anti-Inflammatory (Cortisol, Dehydrocortic Alcohol, dexamethasone, shell cortisol, etc.), excited. Stimulant (methyl amphetamine hydrochloride, methylphenidate hydrochloride, etc.), psychotropic agent (imamine hydrochloride, diazapine, Lefu, hydrochloric acid, fluconate, paroxetine hydrochloride, bromine Hydrogen citalopram, Prozac Hydrochloride, Tridiazepine, Dopamine Antagonist, Clomipramine, Amitriptyline, Dexapride, Anmodipine, Maprotiline, Mise Lin, sputulin, sedative ingot, lofimamine, milnacipran, duloxetine, euphorbia, phenolic ketamine, methotrexate, diazapine, meipubamai, yi Tiazolam, etc., Hormone (espiratory, estriol, progesterone, acetate tacrosterone, metoprolol acetate, acetophenone, etc.), local anesthetic (lidocaine hydrochloride, hydrochloric acid) Novocaine, tetracaine hydrochloride, hydrochloric acid for bcacaine, prilocaine hydrochloride, etc.), urinary organ (Dadoo hydrochloride, tamsulosin hydrochloride, propiverine hydrochloride, etc.), bone relaxant (tizanidine hydrochloride, eperisone hydrochloride, piperazine mesylate, succinylcholine hydrochloride, etc.), genital organ (Litojun hydrochloride, tartaric acid) Epilepsy (dipropyl sodium acetate, clopropine, kappa nitrogen equal), autonomic nerve agent (methyl trimethylamine butyrate, neostigmine bromide, chloride, etc.), anti-Parkinson's disease Agent (pagsulfame methanesulfonate, bromopyridinium mesylate, chlorhexidine hydrochloride, amantadine hydrochloride, pirimidol hydrochloride, helicosine hydrochloride, lactose depressurization, dexcidopa, specific culture Liting, salt Acid dipnin, etc., diuretics (hydrofluoromethyl thiophene, foxima, etc.), respiratory enhancer (L. sylvestris hydrochloride, bismorpholamine, cloproxil hydrochloride, etc.), anti-piling headache agent (methane dihydrogen) Ergotamine, simeptan, ergotamine tartrate, flubenzate hydrochloride, serprestatin hydrochloride, etc., antihistamine (cortisol fumarate, diphenhydramine citrate, chlorpheniramine citrate) Anming, diphenylpyrazine hydrochloride, promethazine hydrochloride, etc., tracheal branch dilating agent (torbutrolol hydrochloride, kefuchuan hydrochloride, salbutamol sulfate, clenbuterol hydrochloride, hydrogen bromide phenoxide) Terbutaline Sulfate, Isoproterenol Sulfate, Formoterol Fumarate, etc., Cardiotonic (Isoproterenol Hydrochloride, Dopamine Hydrochloride, etc.), Coronary Vasodilator (Ditaxan Hydrochloride, Verapamil Hydrochloride) , nitric acid crown ingots, glyceryl trinitrate, nicorandil, etc.), peripheral vasodilator (Chuanzhi sugar ingot, benzyl imidazoline hydrochloride, etc.), non-smoking supplement (nicotine, etc.), circulatory organ (flunzetine hydrochloride) Net, ergipine hydrochloride, Niichuan to be flat, nisoldipine, philoxine, benzene sulfonate Nifludipine, nirvipine hydrochloride, benidipine hydrochloride, enalapril acephate, temocapril hydrochloride, alapril, midazolam hydrochloride, cilazapril, lisino Pu, captopril, trandolapril, tert-butylamine pellipril, attinol, fumarate bisulop, tartaric acid metoprolol, betaxolol hydrochloride, arolol hydrochloride, hydrochloric acid Celilol, Kallithopodol, carteolol hydrochloride, bevanolol hydrochloride, valsartan, candesartan tablets, losartan potassium, knitidine hydrochloride, etc., arrhythmia (Prodamine hydrochloride, dextrosine hydrochloride, nifecaine hydrochloride, mexiladine hydrochloride, Nadulu, Xindaning, etc.), anti-malignant ulcer agent (cyclophosphamide, fluorouracil, Youfu capsule, hydrochloric acid Procarbazine, ramustine, oleino dihydrochloride Ken, Fururijin, etc., anti-lipidemia agents (pravastatin, simvastatin, Benazol, cut bar, etc.), blood sugar lowering agents (Geliben, chlorpropamide, tolbutamide, Sodium gliproclidine, grebazole, dibutyl hydrazine hydrochloride, therapeutic agent for peptic ulcer (proglumide, cetrozine hydrochloride, spirofuranone, cimetidine, glucosinolate) Cholesterol (deoxyurin, acetaminophen, etc.), digestive tract exercise improver (Dopplidu, Hisapur, etc.), liver dysentery (tiopronin, etc.), anti-allergic agent (fumaric acid) Ketotifen, azelastine hydrochloride, etc., antiviral agent (acyclovir, etc.), sedative (sensitive saponin, difenidol hydrochloride, etc.), antibiotic (ceftidine, cefdinir, Cefpodoxime, cefotaxime, clarithromycin, erythromycin, methyl erythromycin, karna sulphate, cycloserine, tetracycline, benzylpenicillin potassium, propisillin, chlorthacillin sodium, amine Benzicillin capsules, ampicillin hydrochloride methyl amyl acetate, carbenicillin sodium, chloramphenicol, etc.), habitual poisoning agents (ammonium cyanide, etc.), appetite suppressants (chlorpheniramine, etc.), Chemotherapeutic agents (barium isonicotinate, ethionamide, pyridoxamine, etc.), blood coagulation accelerator (tidocapril hydrochloride, benzylacetone coumarin potassium), anti-senile dementia (phytosan) , Aiyixin hydrochloride, Taklin, betel nut, octopine, etc.), serotonin receptor antagonizing antiemetic agent (ondansetron hydrochloride, hydrochloric acid, you are strong, ramosetron hydrochloride, hydrochloric acid Zarsyn, etc.), gout therapeutics (colchicine, dipropyl sulfonamide, sulfinpyrazol, etc.), analgesics of anesthetic (phenentrene citrate, morphine sulfate, morphine hydrochloride, codeine phosphate, Cocaine hydrochloride, statin hydrochloride, etc.).

且,此等之藥劑亦可單獨使用,亦可併用2 種類以上,只要是藥學上所容許之鹽即可,當然也包含無機鹽或有機鹽中任一者之形態的藥物。且,藥物包含在塗布液中為基本,但亦能夠在塗布液中不包含藥劑,之後再另外藉由實施於微針之基板上的貫通孔來供給。塗布液中之(A)藥劑的含有量為0.1~80重量%,較佳為1~70重量%,特別佳為5~60重量%。 Moreover, these agents can also be used alone or in combination 2 The above-mentioned type may be a pharmaceutically acceptable salt, and of course, a drug in the form of either an inorganic salt or an organic salt. Further, the drug is basically included in the coating liquid, but the drug may not be contained in the coating liquid, and then supplied through a through hole formed in the substrate of the microneedle. The content of the (A) drug in the coating liquid is 0.1 to 80% by weight, preferably 1 to 70% by weight, particularly preferably 5 to 60% by weight.

塗布液中亦可包含與上述藥劑相異之高分子 化合物。作為該高分子化合物,有舉例如,聚環氧乙烷、聚羥甲纖維素、羥丙纖維素、聚羥丙甲基纖維素、聚甲基纖維素、六碳醣、聚乙二醇、聚乙烯醇、聚乙烯基吡咯烷酮、支鏈澱粉、羧甲基纖維素鈉、硫酸軟骨素、玻尿酸、六碳醣、阿拉伯膠等。 The coating liquid may also contain a polymer different from the above agent Compound. Examples of the polymer compound include polyethylene oxide, polyhydroxymethyl cellulose, hydroxypropyl cellulose, polyhydroxypropylmethyl cellulose, polymethyl cellulose, hexasaccharide, and polyethylene glycol. Polyvinyl alcohol, polyvinyl pyrrolidone, amylopectin, sodium carboxymethylcellulose, chondroitin sulfate, hyaluronic acid, hexose, gum arabic, and the like.

其他,在塗布液中,亦可因應必要,添加作 為溶解補助劑或吸收促進劑之碳酸丙烯酯、克羅他命酮、1-薄荷醇、薄荷油、檸檬烯、己二酸二異丙酯等,或作為藥效補助劑之水楊酸甲酯、乙二醇水楊酸酯、1-薄荷醇、百里酚、薄荷油、壬酸香草、紅辣椒萃取物等。 Others, in the coating liquid, may also be added as necessary A propylene carbonate, a crotonone, a 1-menthol, a peppermint oil, a limonene, a diisopropyl adipate or the like as a dissolution aid or an absorption enhancer, or a methyl salicylate as a medicinal adjuvant , ethylene glycol salicylate, 1-menthol, thymol, peppermint oil, citric acid vanilla, red pepper extract, and the like.

且,在塗布液中,因應必要,亦可添加安定 化劑、抗氧化劑、乳化劑、界面活性劑、鹽類等。界面活性劑亦可為非離子性活性劑、離子性活性劑(陽離子、陰離子、兩性)中之任一者,以安全性之面來說,較期望為通常藥藥品基劑中所使用之非離子性活性劑。更詳細來說,有舉出脂肪酸蔗糖酯等糖醇脂肪酸酯、山梨糖醇酐脂肪酸酯、甘油脂肪酸酯、聚甘油脂肪酸酯、丙二醇脂肪酸 酯、聚氧乙烯山梨糖醇酐脂肪酸酯、聚氧乙烯甘油脂肪酸酯、聚乙二醇脂肪酸酯、聚氧乙烯蓖麻油、聚氧乙烯硬化蓖麻油等。 Moreover, in the coating liquid, if necessary, it is also possible to add stability. Chemical agents, antioxidants, emulsifiers, surfactants, salts, and the like. The surfactant may also be any one of a nonionic active agent and an ionic active agent (cation, anion, amphoteric). In terms of safety, it is more desirable to be used in a conventional pharmaceutical base. Ionic active agent. More specifically, there are sugar alcohol fatty acid esters such as sucrose fatty acid esters, sorbitan fatty acid esters, glycerin fatty acid esters, polyglycerin fatty acid esters, and propylene glycol fatty acids. Ester, polyoxyethylene sorbitan fatty acid ester, polyoxyethylene glycerin fatty acid ester, polyethylene glycol fatty acid ester, polyoxyethylene castor oil, polyoxyethylene hardened castor oil and the like.

其他已知的製劑補助物質,只要其具有塗布 液之塗布中所必要之溶解性及黏度之特徵、以及不會對乾燥後的塗布層之性狀及物性造成有害影響,亦可添加於塗布液中。 Other known formulation supplements as long as they have a coating The solubility and viscosity characteristics required for the application of the liquid, and the harmful effects on the properties and physical properties of the coating layer after drying may not be adversely affected, and may be added to the coating liquid.

塗布液中,為了不使液體滴落,必需要有某 種程度之黏性,具體來說必須要為100~100000cps左右之黏度。塗布液之較佳黏度為100~60000cps,藉由黏度在此範圍,即不須依賴微針44之材質,能夠一次塗布所期望之量的塗布液。且,一般來說,黏度越高,被塗布之塗布液的量有增高之傾向,黏度未滿600cps時,要將最低限之塗布液塗布在微針44上較困難。然而,意外地,為45000cps以上時,反而轉變成所得之塗布層46中之藥劑含量會減少。由如此特徵來看,將塗布液之黏度設在45000cps以上之黏度,由於對應使用藥劑之塗布層46中的藥劑含量並非所期望,且經濟性不佳,故塗布液之黏度設在600~45000cps特別佳。 In the coating liquid, in order not to drip the liquid, it is necessary to have a certain The degree of stickiness must be about 100~100000 cps. The coating liquid preferably has a viscosity of 100 to 60,000 cps, and the viscosity is in this range, that is, the desired amount of the coating liquid can be applied at a time without depending on the material of the microneedles 44. Further, in general, the higher the viscosity, the higher the amount of the coating liquid to be applied is. When the viscosity is less than 600 cps, it is difficult to apply the minimum coating liquid to the microneedles 44. However, unexpectedly, when it is 45,000 cps or more, the amount of the agent in the coating layer 46 obtained by the conversion is reduced. From such a characteristic, the viscosity of the coating liquid is set to a viscosity of 45,000 cps or more. Since the content of the drug in the coating layer 46 corresponding to the use of the drug is not desired, and the economy is not good, the viscosity of the coating liquid is set at 600 to 45000 cps. Especially good.

[實施例] [Examples]

以下,基於實施例來具體說明本發明,但本發明並非限定於以下之實施例中。 Hereinafter, the present invention will be specifically described based on examples, but the present invention is not limited to the following examples.

(實施例1) (Example 1)

製作具備空氣壓縮機、壓縮空氣溫度調節裝置、壓力調節裝置、濕度調節裝置、風量調節裝置及空氣過濾器依序介隔送風管線之微針製劑製造用系統。作為濕度調節裝置,組合中空纖絲模組及恆溫水槽來使用。具體來說,將中空纖絲模組的中空纖絲狀膜之內部,連接成使流動於系統內之氣體會通過,並於中空纖絲模組織之中空纖絲狀膜之外部連接成使由恆溫水槽所供給之一定溫度的水會接觸且與恆溫水槽循環。連接各裝置的送風管線中使用鐵氟龍(登錄商標)管線及矽管線,並在作為阻熱材料之管線的周圍設置氣泡腈系合成橡膠製保溫材料。所使用之各裝置之詳細如以下所述。 A system for manufacturing a microneedle preparation having an air compressor, a compressed air temperature adjusting device, a pressure adjusting device, a humidity adjusting device, an air volume adjusting device, and an air filter sequentially interposing a supply line is produced. As a humidity control device, a hollow fiber module and a constant temperature water tank are used in combination. Specifically, the inside of the hollow fibrillar membrane of the hollow fiber module is connected so that the gas flowing in the system passes through and is connected to the outside of the hollow fibrillar membrane of the hollow filament mold structure. The water of a certain temperature supplied by the constant temperature water tank contacts and circulates with the constant temperature water tank. A Teflon (registered trademark) line and a helium line are used in the air supply line connecting the devices, and a bubble nitrile synthetic rubber heat insulating material is disposed around the line as a heat resistant material. The details of each device used are as follows.

空氣壓縮機:控制壓力0.6~0.8MPa,吐出之空氣量85L/min Air compressor: control pressure 0.6~0.8MPa, air volume 85L/min

壓縮空氣溫度調節裝置:電子冷熱式,設定排出溫度23℃ Compressed air temperature regulator: electronic hot and cold, set discharge temperature 23 ° C

風量調節裝置:設定風量30L/min Air volume adjustment device: set air volume 30L/min

空氣過濾器:聚四氟乙烯製,孔徑0.2μm,有效面積50cm2 Air filter: made of polytetrafluoroethylene, with a hole diameter of 0.2 μ m and an effective area of 50 cm 2

恆溫水槽:循環恆溫水槽 Constant temperature water tank: circulating constant temperature water tank

中空纖絲模組:內建230根內徑1mm,外形1.3mm,長度300mm之氟系離子交換樹脂製的中空纖絲之圓筒形模組 Hollow fiber module: Built-in cylindrical module with hollow fiber filament made of fluorine-based ion exchange resin with inner diameter of 1mm, shape of 1.3mm and length of 300mm

壓力調節裝置:回饋控制精密調節器 Pressure regulator: feedback control precision regulator

將所製作之系統介隔著聚丙烯管線連接於塗布腔室內。作為塗布腔室為使用丙烯酸製腔室。塗布腔室進而以蓬蓋覆蓋,並藉由精密溫濕度元件來管理蓬蓋內之溫濕度。將恆溫水槽設定成23℃,使各裝置啟動。將壓力調節裝置之設定壓力設為0.1~0.3Mpa,在分別之壓力條件下,測定塗布腔室內之相對濕度(%)。將結果表示於表1。藉由以壓力調節裝置控制中空纖絲模組內之壓力,能夠將塗布腔室內調節成70%(RH)以下之任意濕度,並亦能夠調節成30%(RH)左右之中程度之濕度。 The fabricated system was connected to the coating chamber via a polypropylene line. As the coating chamber, an acrylic chamber was used. The coating chamber is then covered with a canopy and the temperature and humidity within the canopy are managed by precision temperature and humidity elements. The constant temperature water tank was set to 23 ° C to start each device. The set pressure of the pressure adjusting device was set to 0.1 to 0.3 MPa, and the relative humidity (%) in the coating chamber was measured under the respective pressure conditions. The results are shown in Table 1. By controlling the pressure in the hollow fiber module with the pressure adjusting device, the coating chamber can be adjusted to any humidity below 70% (RH), and can also be adjusted to a humidity of about 30% (RH).

(實施例2) (Example 2)

使用與實施例1同樣之系統,進行濕度維持試驗。藉由啟動系統之各裝置,並適當地改變壓力調節裝置之設定壓力,來調節塗布腔室內之濕度。經時地測定塗布腔室內之濕度。將結果表示於圖7。在約30%(圖7(a))、約50%(圖7(b))、約70%(圖7(c))分別的濕度中,經過長時間,能夠將塗布腔室內之濕度維持一定。 The humidity maintenance test was carried out using the same system as in Example 1. The humidity in the coating chamber is adjusted by activating the various devices of the system and appropriately changing the set pressure of the pressure regulating device. The humidity in the coating chamber was measured over time. The results are shown in Fig. 7. In a humidity of about 30% (Fig. 7(a)), about 50% (Fig. 7(b)), and about 70% (Fig. 7(c)), the humidity in the coating chamber can be maintained over a long period of time. for sure.

(實施例3) (Example 3)

以實施例1之方法將溫濕度調節成23℃、60%(RH)之塗布腔室內,進行對微針裝置之塗布試驗。塗布試驗之具體方法如以下所述。 The coating test of the microneedle device was carried out by adjusting the temperature and humidity into a coating chamber of 23 ° C and 60% (RH) in the same manner as in Example 1. The specific method of the coating test is as follows.

(微針) (Microneedles)

材質:聚乳酸,高度:500μm,密度:625根/cm2,微針裝置之製劑面積:1cm2/patch Material: polylactic acid, height: 500μm, density: 625/cm 2 , preparation area of microneedle device: 1cm 2 /patch

(塗布液) (coating liquid)

以2質量%之安息香酸鈉,38質量%之六碳醣40,48質量%之甘油,12質量%之純化水的比例來混合,得到塗布液。 The coating liquid was obtained by mixing 2% by mass of sodium benzoate, 38% by mass of hexose carbon 40, 48% by mass of glycerin, and 12% by mass of purified water.

將對微針之塗布液之塗布,以上述之圖6(a)~(c)所示之方法來進行。在設置於塗布腔室內之金屬屏障板(厚度75μm,開口徑250μm,節距400μm)上,將所得之塗布液以刮勺刮過,並填充於金屬屏障板之開口部。藉由於已充填之開口部中插入微針後抽出,將塗布液塗布於微針上。將塗布後的微針風乾後,保存於室溫。塗布於100根的微針裝置上後,在每10根中抽出1根,定量所塗布之安息香酸鈉量。作為安息香酸鈉之定量方法為,將風乾後之微針上的藥劑以1ml的水抽出,將所得之抽出液中的安息香酸鈉濃度使用HPLC來測定。由所得之 測定值算出每1根微針製劑上的含量。將結果表示於圖8。乾燥後之微針上的樣品藥劑之含有量在各方法之間的變動非常地小,安息香酸鈉之平均含量為1.8μg,標準偏差為0.1μg,CV值為7.0%。 The application of the coating liquid for the microneedles is carried out by the method shown in Fig. 6 (a) to (c) above. The resulting coating liquid was scraped off with a spatula and filled in the opening of the metal barrier plate on a metal barrier plate (thickness 75 μm , opening diameter 250 μm , pitch 400 μm ) disposed in the coating chamber. . The coating liquid is applied to the microneedles by inserting the microneedles into the filled opening and extracting them. The coated microneedles were air-dried and stored at room temperature. After being applied to 100 microneedle devices, one was taken out from every 10, and the amount of sodium benzoate applied was quantified. As a method of quantifying sodium benzoate, the drug on the microneedle after air drying was extracted with 1 ml of water, and the concentration of sodium benzoate in the obtained extract was measured by HPLC. The content on each of the microneedle preparations was calculated from the obtained measured values. The results are shown in Fig. 8. The content of the sample drug on the dried microneedle was very small between the methods, and the average content of sodium benzoate was 1.8 μg, the standard deviation was 0.1 μg, and the CV value was 7.0%.

(實施例4) (Example 4)

使用與實施例1相同之系統及圖9所示之塗布腔室,進行風量調節試驗。塗布腔室之大小如以下所述。 The air volume adjustment test was carried out using the same system as in Example 1 and the coating chamber shown in Fig. 9. The size of the coating chamber is as follows.

高度35mm,寬度50mm,長度205mm,容積約0.359L Height 35mm, width 50mm, length 205mm, volume about 0.359L

排氣口(開口)21:長方形,25mm×30mm Exhaust port (opening) 21: rectangular, 25mm × 30mm

連接有送風管線L之給氣口:圓形,直徑16mm Air supply port connected to the air supply line L: round, 16mm in diameter

啟動系統之各裝置,以風量調節裝置將風量設定成表2所示之各值,並因應必要,適當地調節恆溫水槽溫度、循環水量及壓縮空氣溫度。在塗布腔室內設置中央與四個角落共計5個的測定位置p,分別設為塗布腔室之高度的2分之1之高度的位置。在各測定位置p中測定濕度,求出5點之平均濕度、標準偏差(SD)及CV值。將結果表示於表2。雖然風量不管在任何值下,皆能任意地調節其濕度,但風量在一定量以上時,能夠更均勻地調節塗布腔室內之濕度。 Each device of the system is started, and the air volume is set to the values shown in Table 2 by the air volume adjusting device, and the temperature of the constant temperature water tank, the circulating water volume, and the compressed air temperature are appropriately adjusted as necessary. In the coating chamber, a total of five measurement positions p at the center and four corners are provided, and each is set to a height of one-half of the height of the coating chamber. The humidity was measured at each measurement position p, and the average humidity, standard deviation (SD), and CV value at five points were obtained. The results are shown in Table 2. Although the air volume can adjust the humidity arbitrarily at any value, the humidity in the coating chamber can be more uniformly adjusted when the air volume is more than a certain amount.

(比較例1) (Comparative Example 1)

製作依序具備空氣壓縮機、壓縮空氣溫度調節裝置、風量調節裝置、空氣過濾器及濕度調節裝置之微針製劑製造用系統。各裝置中有關與實施例1共通者即使用與實施例1相同者。將所製作之微針製劑製造用系統與實施例1相同地,介隔著聚丙烯管線而與丙烯酸製塗布腔室連接。塗布腔室進而以蓬蓋覆蓋,並藉由精密溫濕度元件來管理蓬蓋內之溫濕度。使各裝置啟動,並將塗布腔室內充滿已調節溫濕度的空氣。 A system for manufacturing a microneedle preparation having an air compressor, a compressed air temperature adjusting device, an air volume adjusting device, an air filter, and a humidity adjusting device is sequentially manufactured. In the respective devices, the same as in the first embodiment, the same as in the first embodiment. The system for producing a microneedle preparation produced in the same manner as in Example 1 was connected to an acrylic coating chamber via a polypropylene line. The coating chamber is then covered with a canopy and the temperature and humidity within the canopy are managed by precision temperature and humidity elements. The devices are activated and the coating chamber is filled with air having a regulated temperature and humidity.

經時測定塗布腔室內之溫度及濕度。將結果表示於圖10(a)、(b)。在比較例1之系統中,雖然能夠將塗布腔室內之溫度及濕度調節成所期望之範圍,但即使將循環於中空纖絲模組內的水之溫度下降,要在濕度下降到未滿70%(RH)之狀態下使之安定是相當困難的。 The temperature and humidity in the coating chamber were measured over time. The results are shown in Figures 10(a) and (b). In the system of Comparative Example 1, although the temperature and humidity in the coating chamber can be adjusted to a desired range, even if the temperature of the water circulating in the hollow fiber module is lowered, the humidity is lowered to less than 70. It is quite difficult to stabilize it in the state of %(RH).

(比較例2) (Comparative Example 2)

介隔著送風管線,依序連接空氣壓縮機、風量調節裝置及濕度調節裝置。空氣壓縮機及風量調節裝置使用與實施例1相同者,同樣地進行設定。作為濕度調節裝置僅使用循環恆溫水槽。測量塗布腔室內之溫度及相對濕度的經過。將結果表示於圖11(a)、(b)。塗布腔室內之溫度可以看出在日後及日內中的變動。且,塗布腔室內之相對濕度也有大幅之變動。 The air compressor, the air volume adjusting device and the humidity adjusting device are sequentially connected through the air supply line. The air compressor and the air volume adjusting device were used in the same manner as in the first embodiment, and were set in the same manner. As the humidity control device, only the circulating constant temperature water tank is used. The temperature and relative humidity of the coating chamber were measured. The results are shown in Figures 11(a) and (b). The temperature in the coating chamber can be seen as a change in the future and in the day. Moreover, the relative humidity in the coating chamber also varies greatly.

10‧‧‧空氣壓縮機 10‧‧‧Air compressor

12‧‧‧壓縮空氣溫度調節裝置 12‧‧‧Compressed air temperature regulator

14‧‧‧風量調節裝置 14‧‧‧Air volume adjustment device

16‧‧‧空氣過濾器 16‧‧‧Air filter

18‧‧‧濕度調節裝置 18‧‧‧Humidity control device

20‧‧‧塗布腔室 20‧‧‧ Coating chamber

21‧‧‧開口 21‧‧‧ openings

22‧‧‧水分供給器 22‧‧‧Water supply

24‧‧‧透濕膜裝置 24‧‧ ‧ wet film device

26‧‧‧溫濕度探測器(溫度探測器及濕度探測器) 26‧‧‧ Temperature and Humidity Detector (Temperature Detector and Humidity Detector)

28‧‧‧控制裝置(第1~第6控制手段) 28‧‧‧Control device (1st to 6th control means)

30‧‧‧壓力調節裝置 30‧‧‧ Pressure regulating device

200‧‧‧微針製劑製造用系統 200‧‧‧Microneedle preparation system

L‧‧‧送風管線 L‧‧‧Air supply line

Claims (13)

一種微針製劑製造用系統,其係調節塗布腔室內之空氣環境的微針製劑製造用系統,該塗布腔室內的空氣環境係用於將包含藥劑之塗布液塗布於微針來製造微針製劑,且調節塗布腔室內之空氣環境的微針製劑製造用系統,其特徵為具備空氣壓縮機;與用來調節由前述空氣壓縮機所供給之空氣的濕度,且前述空氣與作為濕度調節源之水分會被透濕膜所分離之透濕膜型的濕度調節裝置;與調節由前述空氣壓縮機所供給之空氣的壓力之壓力調節裝置;與將供給至該塗布腔室內的空氣除菌之空氣過濾器。 A system for manufacturing a microneedle preparation, which is a system for manufacturing a microneedle preparation for adjusting an air environment in a coating chamber, wherein an air environment in the coating chamber is used for applying a coating liquid containing a drug to a microneedle to manufacture a microneedle preparation And a system for manufacturing a microneedle preparation for adjusting an air environment in a coating chamber, characterized by comprising an air compressor; and for adjusting a humidity of the air supplied by the air compressor, and the air and the humidity adjusting source a moisture permeable membrane type humidity modulating device in which moisture is separated by a moisture permeable membrane; a pressure regulating device for regulating the pressure of the air supplied by the air compressor; and air sterilizing air supplied to the coating chamber filter. 如請求項1之微針製劑製造用系統,其中,前述透濕膜被形成為中空纖絲狀者。 The system for producing a microneedle preparation according to claim 1, wherein the moisture permeable film is formed into a hollow fibrillar shape. 如請求項1或2之微針製劑製造用系統,其中,具備濕度探測器、與基於對應於前述濕度探測器所檢測出之濕度的信號,來控制前述壓力調節裝置之第1控制手段。 The system for producing a microneedle preparation according to claim 1 or 2, comprising: a humidity detector; and a first control means for controlling the pressure adjusting means based on a signal corresponding to the humidity detected by the humidity detector. 如請求項1~3中任一項之微針製劑製造用系統,其中,具備溫度探測器、與基於對應於前述溫度探測器所檢測出之溫度的信號,來控制前述壓力調節裝置之第2控制手段。 The system for producing a microneedle preparation according to any one of claims 1 to 3, further comprising: a temperature detector and a signal based on a temperature corresponding to the temperature detector to control the second pressure regulating device Control means. 如請求項1~4中任一項之微針製劑製造用系統, 其中,具備調節由前述空氣壓縮機所供給之空氣的溫度之壓縮空氣溫度調節裝置。 The system for manufacturing a microneedle preparation according to any one of claims 1 to 4, Among them, there is provided a compressed air temperature adjusting device that adjusts the temperature of the air supplied by the air compressor. 如請求項5之微針製劑製造用系統,其中,具備濕度探測器、與基於對應於以前述濕度探測器所檢測出的濕度之信號,來控制前述壓縮空氣溫度調節裝置之第3控制手段。 A system for producing a microneedle preparation according to claim 5, comprising: a humidity detector; and a third control means for controlling the compressed air temperature adjusting means based on a signal corresponding to the humidity detected by the humidity detector. 如請求項5或6之微針製劑製造用系統,其中,具備溫度探測器、與基於對應於前述溫度探測器所檢測出的溫度之信號,來控制前述壓縮空氣溫度調節裝置之第4控制手段。 The system for producing a microneedle preparation according to claim 5 or 6, wherein the fourth control means for controlling the compressed air temperature adjusting means is provided with a temperature detector and a signal based on a temperature corresponding to the temperature detector . 如請求項1~7中任一項之微針製劑製造用系統,其中,前述濕度調節裝置具備供給水分之水分供給器。 The system for producing a microneedle preparation according to any one of claims 1 to 7, wherein the humidity control device includes a moisture supply device that supplies moisture. 如請求項8之微針製劑製造用系統,其中,前述水分供給器為恆溫水槽。 The system for producing a microneedle preparation according to claim 8, wherein the moisture supply device is a constant temperature water tank. 如請求項8或9之微針製劑製造用系統,其中,前述水分供給器為能夠調節水溫者。 The system for producing a microneedle preparation according to claim 8 or 9, wherein the moisture supplier is a person capable of adjusting the water temperature. 如請求項10之微針製劑製造用系統,其中,具備濕度探測器、與基於對應於前述濕度探測器所檢測出的濕度之信號,來控制前述水分供給器之水溫之第5控制手段。 The system for producing a microneedle preparation according to claim 10, comprising: a humidity detector; and a fifth control means for controlling the water temperature of the moisture supplier based on a signal corresponding to the humidity detected by the humidity detector. 如請求項10或11之微針製劑製造用系統,其中,具備溫度探測器、與基於對應於前述溫度探測器所檢測出的溫度之信號,來控制前述水分供給器之水溫之第6控制手段。 The system for manufacturing a microneedle preparation according to claim 10 or 11, comprising a temperature detector and a sixth control for controlling the water temperature of the moisture supplier based on a signal corresponding to a temperature detected by the temperature detector means. 一種空調方法,其係用於調節塗布腔室內之空氣環境的空調方法,該塗布腔室內之空氣環境係用於將包含藥劑之塗布液塗布於微針來製造微針製劑,其特徵為包含:以前述空氣與作為濕度調節源之水分會被透濕膜所分離之透濕膜型的濕度調節裝置,來調節送入前述塗布腔室之空氣的濕度之步驟;與以壓力調節裝置來調節送入該塗布腔室之空氣的壓力之步驟;與以空氣過濾器來將前述空氣除菌之步驟;與將濕度經調節且除菌之前述空氣導入前述塗布腔室之步驟。 An air conditioning method for adjusting an air environment in a coating chamber, wherein an air environment in the coating chamber is used to apply a coating liquid containing a medicament to a microneedle to manufacture a microneedle preparation, which comprises: a step of adjusting the humidity of the air sent to the coating chamber by the moisture-adjusting membrane type humidity adjusting device in which the air and the moisture adjusting source are separated by the moisture-permeable membrane; and adjusting the sending by the pressure adjusting device a step of introducing air into the coating chamber; a step of sterilizing the air with an air filter; and a step of introducing the humidity-conditioned and sterilized air into the coating chamber.
TW103118824A 2013-05-29 2014-05-29 Microneedle preparation system and air conditioning method TWI636781B (en)

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