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WO2024017300A1 - System for preparing mrna liposomes and use thereof - Google Patents

System for preparing mrna liposomes and use thereof Download PDF

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Publication number
WO2024017300A1
WO2024017300A1 PCT/CN2023/108173 CN2023108173W WO2024017300A1 WO 2024017300 A1 WO2024017300 A1 WO 2024017300A1 CN 2023108173 W CN2023108173 W CN 2023108173W WO 2024017300 A1 WO2024017300 A1 WO 2024017300A1
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WO
WIPO (PCT)
Prior art keywords
unit
sterile
liquid
mrna
encapsulation unit
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Application number
PCT/CN2023/108173
Other languages
French (fr)
Chinese (zh)
Inventor
吴守亮
毛叶飞
徐丙良
Original Assignee
浙江健新原力制药有限公司
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Publication date
Application filed by 浙江健新原力制药有限公司 filed Critical 浙江健新原力制药有限公司
Priority to CN202380012307.0A priority Critical patent/CN117597110A/en
Publication of WO2024017300A1 publication Critical patent/WO2024017300A1/en

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Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K45/00Medicinal preparations containing active ingredients not provided for in groups A61K31/00 - A61K41/00
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/10Dispersions; Emulsions
    • A61K9/127Liposomes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/58Multistep processes

Definitions

  • This application belongs to the field of liposome technology, and specifically relates to a system for preparing mRNA liposomes and its application.
  • mRNA technology products are based on the "central dogma" of mRNA guiding protein synthesis. They are designed and synthesized in vitro containing mRNA sequences encoding specific antigens. After sequence optimization, chemical modification and purification, they are delivered to human cells in different ways and are translated by the body's cells. Produce proteins, induce immune responses, supplement body proteins, regulate immunity, etc., thereby preventing or treating diseases. It has a wide range of applications, including the preparation of infectious disease vaccines, tumor immunotherapy, monoclonal antibody drug substitution, and other protein drug substitution. At present, the fastest-growing and most widely used vaccines are preventive vaccines for infectious diseases.
  • the mRNA vaccine represented by BNT162b2 produced by Pfizer has shined in the application of COVID-19.
  • mRNA drugs There are many areas for improvement in the current production of mRNA drugs. For example: 1) Since the mRNA drug will be infused back into the patient, it is an injection grade. According to Pharmacopoeia IV, the level of sterility control is extremely high, so its preparation process requires very high sterility control of the environment, personnel, and equipment; 2 ) When the conventional production process produces different samples at the same time, it is easy to cause cross-contamination through equipment, environment, and personnel, which makes it impossible to achieve multi-variety collinear production of products. The production of gene therapy products itself has small scale, high quality requirements, and demand.
  • the purpose of this application is to provide a system for preparing mRNA liposomes and its application.
  • the pipelines through which the raw materials, intermediate products and final products flow are fully closed, which can effectively avoid contamination and cross-contamination, reduce the number of sterilization filtrations, and reduce the environmental impact. , equipment, personnel and other external factors on cell products, and improve the quality and stability of the products.
  • the present application provides a system for preparing mRNA liposomes, which system follows the connection sequence. It includes liquid preparation unit, encapsulation unit, liquid replacement unit and preparation unit;
  • the system is a fully closed system.
  • the "unit” in this application may be an instrument or equipment, or a set of instruments or equipment capable of completing a certain work. These different units can form a system with specific functions.
  • mRNA liposomes are also known as “mRNA-liposome complexes", “mRNA-lipid nanocomplexes”, “mRNA-liposome nanocomplexes”, “lipid nanocomplexes” “Plastid-mRNA complex”, etc., is a lipid nanoparticle (Lipid nanoparticle, LNP) prepared by methods including but not limited to film hydration method, extrusion method, homogenization method, microfluidics, etc.
  • the surface of LNP is mainly neutral lipids and PEGylated lipids as well as partially ionizable cationic lipids and cholesterol; inside the core, ionizable cationic lipids and cholesterol are present.
  • mRNA messenger RNA
  • mRNA refers to a polynucleotide encoding at least one polypeptide.
  • mRNA includes modified and unmodified RNA.
  • An mRNA may contain one or more coding and non-coding regions.
  • the present invention can be used to encapsulate any mRNA.
  • the liquid preparation unit in this application can be a conventional liquid preparation tank in this field, optionally, it is equipped with a conventional stirring device or a magnetic stirring device.
  • the functions of the liquid preparation unit in this application include but are not limited to dissolving an appropriate concentration of mRNA buffer in a slightly acidic solution to form an aqueous phase, and dissolving lipids in ethanol to form an organic phase.
  • the liquid preparation unit can prepare the aqueous phase and the organic phase according to conventional preparation methods in the art, so that they have sufficient composition characteristics to form mRNA liposomes.
  • the preparation of the mRNA stock solution may be routine in the art, and may include, for example, a series of steps such as in vitro transcription, post-transcriptional modification, enzyme treatment, chromatography purification, concentration and medium replacement, and stock solution preparation.
  • the instruments/equipment used to perform this series of steps can all be conventional in the art, and they constitute the unit for preparing the mRNA stock solution.
  • the liquid preparation unit also has the function of remelting the original mRNA solution.
  • Instruments/equipment used for refusion may be routine in the art.
  • Various methods can be used to prepare mRNA solutions suitable for use in the present invention.
  • the mRNA can be dissolved directly in the buffer solutions described herein.
  • the mRNA solution can be produced by mixing the mRNA stock solution with a buffer solution before mixing with the organic phase for encapsulation.
  • the liquid preparation unit can also mix the mRNA stock solution and the buffer solution.
  • the organic phase contains a mixture of lipids suitable for forming lipid nanoparticles for encapsulating mRNA.
  • a suitable organic phase is ethanol-based.
  • a suitable organic phase may contain a mixture of desired lipids dissolved in pure ethanol (ie, 100% ethanol).
  • a suitable organic phase is isopropyl alcohol based.
  • a suitable organic phase is based on dimethyl sulfoxide.
  • a suitable organic phase is a mixture of suitable solvents including, but not limited to, ethanol, isopropanol, and dimethyl sulfoxide.
  • the organic phase includes one or more cationic lipids, one or more helper lipids, and one or more PEG-modified lipids. In some embodiments, the organic phase further includes one or more cholesterol-based lipids. In some embodiments, the one or more cholesterol-based lipids are cholesterol and/or PEGylated cholesterol. In some embodiments, the organic phase includes preformed lipid nanoparticles. In some embodiments, the organic phase is a suspension of preformed lipid nanoparticles.
  • a suitable organic phase may contain a mixture of various concentrations of the desired lipids.
  • a suitable organic phase may contain a mixture of the desired lipids at a total concentration equal to or greater than about 0.1 mg/ml, 1.0 mg/ml, 10 mg/ml, or 100 mg/ml.
  • the liquid preparation unit also has the function of controlling the ratio of the aqueous phase and the organic phase.
  • Any desired lipids can be mixed in any ratio suitable for encapsulating mRNA.
  • a suitable organic phase contains a mixture of desired lipids including cationic lipids, accessory lipids (e.g., non-cationic lipids and/or cholesterol lipids), and/or PEG oxidized lipids.
  • a suitable organic phase contains a mixture of desired lipids including one or more cationic lipids, one or more accessory lipids (e.g., non-cationic lipids and /or cholesterol lipids) and one or more PEGylated lipids.
  • the lipids in this application can be conventional in the art, including but not limited to cationic lipids (such as ALC-0315, CAS: 2036272-55-4), cholesterol, auxiliary lipids (such as DOPE), and polyethylene glycol. Alcoholized phospholipids (such as PEG2000-DMG), etc.
  • the functions of the cationic lipid include, but are not limited to, binding to negatively charged mRNA and efficiently entrapping mRNA drugs.
  • the functions of cholesterol include, but are not limited to, stabilizing the structure of the mRNA liposomes and improving the stability of the mRNA liposomes by regulating the fluidity of the membrane.
  • auxiliary lipid include, but are not limited to, stabilizing mRNA liposomes and improving the efficiency of delivering mRNA.
  • the functions of the PEGylated phospholipids include, but are not limited to, improving the stability of mRNA liposomes, reducing their binding to plasma proteins, and prolonging their circulation time in the body.
  • the selection of cationic lipids, helper lipids, cholesterol-based lipids, and/or PEG-modified lipids comprising lipid nanoparticles, and the relative molar ratios of these lipids to each other are based on the selection Characteristics of the lipids, the nature of the intended target cells, and the characteristics of the mRNA to be delivered. Other considerations include, for example, the saturation of the alkyl chain and the size, charge, pH, pKa, fusogenicity, and toxicity of the selected lipid. Therefore, the molar ratio can be adjusted accordingly.
  • the liquid preparation unit in this application is an explosion-proof liquid preparation unit.
  • the function of the explosion-proof liquid dispensing unit This can include, but is not limited to, effectively avoiding safety hazards caused by using high-concentration ethanol solutions during the preparation of the organic phase.
  • the explosion-proof liquid dispensing unit may be conventional in the field, such as a stainless steel explosion-proof liquid dispensing tank.
  • the functions of the encapsulation unit include but are not limited to controlling the injection temperature, pressure, flow rate and ratio of the two-phase solution, etc., and use the film hydration method, extrusion method, homogenization method, ultrasonic wave, shearing or Microfluidic mixing and other LNP preparation methods are used to prepare mRNA liposomes.
  • the encapsulation unit in this application is a microfluidic encapsulation unit, which prepares mRNA liposomes through a microfluidic mixing method.
  • An example of the operation of the microfluidic encapsulation unit is that the organic phase and the aqueous phase are mixed by jet collision. At the same time, the ethanol in the organic phase is diluted, the pH of the solution changes, and the liposomes separate out to form lipid nanoparticles and interact with the mRNA. Formation of encapsulated complexes.
  • the structure of the microfluidic encapsulation unit can be conventional in the art, for example, it includes a high-pressure pump and a cavity.
  • the high-pressure pump is used to form two jets of the aqueous phase and the organic phase, and the process is carried out in the cavity. Hedge.
  • the flow rate of the liquid buffer during the preparation of mRNA liposomes through the microfluidic encapsulation unit is controllable.
  • the diameter of at least one of the reservoirs, conduits, and/or connectors in the microfluidic chip can be controlled to achieve desired flow rates and resulting mixing properties. The larger the diameter of the conduit, the greater the flow of liquid through the conduit.
  • flow limiting settings are employed in the microfluidic chip to achieve the desired flow rate and resulting mixing properties.
  • the process of preparing mRNA liposomes by the microfluidic encapsulation unit described in this application is sterile.
  • the microfluidic encapsulation units described herein are not in a sterile environment.
  • the microfluidic encapsulation unit allows reproducible encapsulation of mRNA in lipids.
  • the microfluidic encapsulation unit allows reproducible production of lipid nanoparticles (LNPs).
  • microfluidic encapsulation unit can be selected from Genizer, Precision NanoSystems (PNI), PreciGenome, Dolomite Microfluidics, Myanna (Shanghai) Instrument Technology Co., Ltd., and Suzhou Aitson Pharmaceutical Equipment Co., Ltd., etc.
  • the product obtained by the encapsulation unit in addition to the mRNA liposome, there are also impurities such as unused mRNA or its fragments, unused lipids, ethanol, and possible microorganisms.
  • impurities such as unused mRNA or its fragments, unused lipids, ethanol, and possible microorganisms.
  • the above-mentioned impurities are removed using the liquid exchange unit in this application to obtain purified mRNA liposomes, and preparations can be made according to the function or formula requirements of the mRNA liposomes, for example, adding ingredients to facilitate long-term stable storage of the product and Excipient ingredients (such as sucrose) that exert the medicinal effect.
  • the liquid exchange unit in this application is a tangential flow filtration liquid exchange unit.
  • Tangential Flow Filtration also known as Cross Flow Filtration, refers to the flow of liquid
  • the filtration form is perpendicular to the filtration direction. It is driven by pressure and performs membrane separation based on molecular size.
  • the cutoff pore size of the membrane in the tangential flow filtration unit described in this application can be determined based on the particle size of the prepared mRNA liposomes.
  • tangential flow filtration is that the non-permeable retentate or "filter cake" that can collect within the filter and clog it during traditional "dead-end” filtration is instead transported along the surface of the filter. This advantage makes tangential flow filtration particularly suitable for large-scale purification of mRNA liposomes.
  • transmembrane pressure differential is the force that pushes fluid through the filter, carrying permeable molecules with it.
  • Feed rate also called cross-flow rate
  • the feed rate determines the force that removes molecules that might otherwise clog or foul the filter and thereby limit the filtrate flow rate.
  • the permeate flow rate is the rate at which permeate is removed from the system. For a constant feed rate, increasing the permeate flow rate increases the pressure across the filter, resulting in an increase in filtration rate, and may also increase the risk of filter clogging or fouling.
  • the total sealing described in this application can be achieved through a one-time sealing process.
  • the aseptic connector can be a sterile connector or a sterile takeover machine; depending on the disconnected connection unit, the blocker can be a sterile disconnector or a sterile disconnector.
  • Bacteria sealing tube machine can be used to connect/disconnect different units.
  • the area of the sterile area, especially the core sterile production area is reasonably designed to reduce the cost of sterility assurance.
  • the formulation unit is in the Class C zone.
  • the fluid exchange unit and the preparation unit are in the Class C zone.
  • the fluid exchange unit and the preparation unit are in the Class C zone.
  • the system in order of connection, is an explosion-proof liquid preparation unit, a sterile connector/sterile disconnector, a microfluidic encapsulation unit, a sterile take-over machine/a sterile tube sealing machine, TFF liquid changing unit, sterile tube taking machine/sterile sealing machine and liposome preparation unit.
  • the connection sequence of each unit described in this application is preferably consistent with the steps in large-scale production.
  • connection between the liquid preparation unit and the encapsulation unit is achieved through a sterile connector.
  • the disconnection between the dispensing unit and the encapsulating unit is achieved by a sterile disconnect.
  • connection between the fluid mixing and encapsulation unit and the liquid exchange unit is achieved through a sterile pipe machine.
  • the disconnection between the fluid mixing and encapsulation unit and the fluid exchange unit is accomplished by a sterile sealing machine.
  • connection between the liquid changing unit and the preparation unit is realized through a sterile pipe machine.
  • the disconnection between the liquid exchange unit and the preparation unit is achieved by a sterile sealing machine.
  • linkers and blockers described in this application can effectively connect different units, enabling the preparation of mRNA liposomes to realize an integrated production process of mRNA liposomes for the first time in this field, overcoming the quality inspection of different suppliers.
  • the device lacks integration and connection defects between devices.
  • Sterile connectors/sterile disconnectors as described in this article allow for quick and easy sterile connection and disconnection, even in non-sterile environments.
  • the sterile connector/disconnector can act as a sterile filter to filter the solution.
  • the system does not include additional sterile filters after the sterile connector/sterile disconnector.
  • a filter is provided as a sterilizing filter after the explosion-proof liquid preparation unit.
  • the number of other sterilizing filters connected after the explosion-proof liquid preparation unit is less than 5. In some embodiments, in the system, the number of other sterilizing filters connected after the explosion-proof liquid preparation unit is less than 3. In some embodiments, in the system, the number of other sterilizing filters connected after the explosion-proof liquid preparation unit is less than 1.
  • the number of sterile filters in the system is less than 5. In certain embodiments, the number of sterile filters in the system is less than 4. In certain embodiments, the number of sterile filters in the system is less than 3. In certain embodiments, the number of sterile filters in the system is less than 2. In certain embodiments, the number of sterile filters in the system is less than 1.
  • the system in this application further includes a unit for preparing plasmid DNA stock solution and a unit for preparing mRNA stock solution upstream of the liquid preparation unit.
  • the connection/disconnection between such units for preparing raw solutions and between them and the liquid dispensing unit is achieved through sterile connectors/sterile disconnectors.
  • the preparation of the plasmid DNA stock solution may be routine in the art, and may include steps such as fermentation culture, harvesting and clarification, refining and purification, linearization, and filtration and aliquots.
  • the instruments/equipment used to perform this series of steps can all be conventional in the art, for example Bacterial culture fermentation tanks, CO 2 incubators, centrifuges, and equipment for tangential flow filtration or depth filtration, etc., constitute the unit for preparing plasmid DNA stock solution.
  • system in the present application further includes a unit downstream of the preparation unit for preparing cell therapy-related products using the prepared mRNA liposomes.
  • the present application provides a method for preparing mRNA liposomes, which includes preparing using a system as described in the first aspect.
  • the following operations can be performed in sequence: explosion-proof docking, fluid docking, sample sampling, buffer storage and transfer, and sample solution storage and transfer.
  • each unit in this application can be a mature process in the field, such as using a liquid preparation unit to prepare two phases and using an encapsulation unit to encapsulate mRNA.
  • the system described in this application is a fully closed system.
  • a one-time closed process can be used during use to effectively avoid contamination and cross-contamination, reduce the number of sterilization filtrations, and reduce the impact of the environment, equipment, personnel, and other external factors on cell products. impact, increase production and improve product stability.
  • the system described in this application reasonably divides each unit into an explosion-proof area and a Class C area.
  • the explosion-proof liquid preparation unit and the encapsulation unit constitute an explosion-proof area
  • the liquid replacement unit and the preparation unit constitute a Class C area.
  • the system of this application contains an explosion-proof liquid dispensing unit, it can provide an explosion-proof production environment and effectively prevent explosions.
  • the purification, preparation, and packaging processes are carried out in clean areas of Class C or higher, so that there is no microbial contamination during the purification, preparation, and packaging processes.
  • Aseptic connection/disconnection is adopted between the explosion-proof area and the C-level area.
  • the equipment in the C-level area does not need to be sterilized multiple times during the entire process, which greatly simplifies the production process.
  • the equipment in the Class C area does not need to be sterilized after the explosion-proof docking and/or fluid docking steps.
  • the equipment in the Level C zone is sterilized less than 10 times during each intermittent production process. In some embodiments, the equipment in the Level C zone is sterilized less than 5 times during each intermittent production process. In some embodiments, the equipment in the Level C zone is sterilized less than 4 times during each intermittent production process. In some embodiments, the equipment in the Level C zone is sterilized less than three times during each intermittent production process. In some embodiments, the equipment in the Level C zone is sterilized less than twice during each intermittent production process. In some embodiments, the equipment in the Level C zone is sterilized less than once during each intermittent production process.
  • systems as described herein can be used in continuous production processes.
  • the frequency of sterilization treatment of equipment in the Class C area during continuous production is less than 10 times per day.
  • the equipment in the Level C zone is sterilized less than 5 times per day during the continuous production process.
  • the equipment in the Level C zone is sterilized less than 4 times per day during the continuous production process.
  • the equipment in the Level C zone is sterilized less than three times per day during the continuous production process.
  • the equipment in the Level C zone is sterilized less than 2 times per day during the continuous production process.
  • the equipment in the Level C zone is sterilized less than once per day during the continuous production process.
  • the system for preparing mRNA liposomes provided in this application provides new ideas for the cooperative development of integrated equipment for mRNA liposomes.
  • Figure 1 shows the system used to prepare mRNA liposomes in Example 1 of the present application.
  • Figure 2 shows a liquid storage bag that transfers liquid to be liquid from the liquid explosion-proof dispensing unit to the encapsulation unit.
  • FIG. 3 shows the TFF fluid exchange unit.
  • Figure 4 shows a sample storage bag used to transfer samples.
  • Figure 5 shows a formulation storage bag for transferring and filling formulations.
  • Example 1 Composition of a system for preparing mRNA liposomes
  • the system mainly consists of an explosion-proof liquid preparation unit (1), a microfluidic encapsulation unit (2), a TFF liquid replacement unit (3) and a preparation unit (4).
  • the explosion-proof liquid preparation unit and microfluidic encapsulation unit constitute the explosion-proof area
  • the TFF liquid replacement unit and preparation unit constitute the C-level area (see Figure 1).
  • the explosion-proof liquid preparation unit (1) and the microfluidic encapsulation unit (2) are connected/disconnected using a sterile connector/sterile disconnector.
  • Figure 2 provides a liquid storage bag that transfers the liquid to be encapsulated from the liquid explosion-proof dispensing unit to the encapsulation unit (2).
  • Liquid such as mRNA solution
  • the filter (57) can filter the liquid flowing into the dosing unit.
  • the liquid storage bag (51) is equipped with a sampling head (55). The sampling head can conveniently extract the solution from the liquid storage bag (51).
  • the liquid storage bag inlet conduit (52) and the liquid storage bag outlet conduit (54) can be thermoplastic tubes, including but not limited to silicone tube, and wait. If required, thermoplastic tubing can be used for aseptic welding for liquid transfer.
  • the port of the liquid storage bag outlet conduit (54) is equipped with an air filter head (56) to prevent the entry of pollutants in the air, especially bacteria.
  • Pipe clamps (53) are installed on the liquid storage bag liquid inlet conduit (52) and the liquid storage bag liquid outlet conduit (54) to control the opening and closing of the pipelines.
  • the liquid storage bag (51) can be connected to the microfluidic encapsulation unit (2) through the liquid storage bag outlet conduit (54).
  • the microfluidic encapsulation unit and the TFF liquid change unit, as well as the TFF liquid change unit and the preparation unit, are connected/disconnected using a sterile takeover machine/sterile tube sealing machine.
  • Figure 3 shows the TFF fluid exchange unit.
  • the liquid inlet conduit (32) can be connected/disconnected from the microfluidic encapsulation unit (2) through a sterile tube taking machine/sterile tube sealing machine.
  • the reflux fluid conduit (33) can be connected/disconnected from the preparation unit (3) through a sterile tube taking machine/sterile tube sealing machine.
  • the mRNA liposomes prepared by the microfluidic encapsulation unit flow into the tangential flow filter (31) through the liquid inlet conduit (32).
  • the permeate flows into and out of the tangential flow filter (31) through the permeate conduit (34) to filter impurities in the preparation.
  • the sample storage liquid shown in Figure 4 can also be passed between the microfluidic encapsulation unit (2) and the TFF liquid replacement unit (3).
  • the bag (61) transfers liquid.
  • Both the sample liquid storage bag liquid inlet conduit (62) and the sample liquid storage bag liquid outlet conduit (64) can be thermoplastic tubes, which can be used for aseptic welding to transfer liquid.
  • the liquid inlet conduit (62) of the sample liquid storage bag and the liquid outlet of the microfluidic encapsulation unit (2) can be connected/disconnected through a sterile take-over machine/sterile sealing machine, and the liquid outlet of the sample liquid storage bag
  • the conduit (64) and the liquid inlet conduit (32) can be connected/disconnected through a sterile tube taking machine/sterile tube sealing machine.
  • the TFF liquid changing unit (3) and the preparation unit (4) are connected/disconnected using a sterile tube taking machine/sterile tube sealing machine. Liquid can also be transferred between the TFF liquid changing unit (3) and the preparation unit (4) through the preparation liquid storage bag (71) as shown in Figure 5.
  • the liquid inlet conduit (72) of the preparation liquid storage bag can be connected/disconnected from the TFF liquid exchange unit (3) through a sterile tube taking machine/sterile tube sealing machine.
  • the preparation in the preparation storage bag (71) flows to the filling needle (75) through the filling pump tube (74), where a peristaltic pump can be installed on the filling pump tube (74) to pump liquid.
  • the ⁇ bag (76) is placed outside the filling pump tube (74) and the filling needle (75).
  • the contact areas between the bag body and the filling pump tube (74) are connected by welding to ensure that the ⁇ bag is fully enclosed. ;
  • the beta valve (77) of the rapid transfer interface (RTP) is attached to the beta bag so as to be aseptically connected to the preparation unit (4).
  • Example 2 Method of use of system for preparing mRNA liposomes
  • the sampling heads (55) and (65) can take samples for monitoring.
  • the pipe clamp (53) of the storage bag can be closed to store the buffer solution.
  • the pipe clamp (53) of the liquid storage bag can be opened and the buffer can be transferred through the sterile docking of the liquid storage bag outlet conduit (54).
  • the sample liquid storage bag pipe clamp (63) can be closed to store the sample liquid.
  • the pipe clamp (63) of the sample storage bag can be opened and connected aseptically through the outlet conduit (64) of the sample storage bag to transfer the sample liquid.
  • Step 1 Remelt the original mRNA solution in the explosion-proof liquid preparation unit (1), and prepare the aqueous phase containing the mRNA solution and the organic phase used to encapsulate the mRNA.
  • Step 2 The solution prepared by the explosion-proof liquid preparation unit is filtered by the filter (57) and then flows into the liquid storage bag (51).
  • Step 2.1 Optionally, open the sampling head (55) to sample and detect the solution in the liquid storage bag (51).
  • Step 3 Pump the solution in the liquid storage bag (51) into the encapsulation unit (2), such as a microfluidic encapsulation unit.
  • the encapsulation unit encapsulates the mRNA to form liposomes.
  • Step 4 Introduce the encapsulated liposome solution into the liquid replacement unit (3).
  • the liquid inlet conduit (32) can be directly connected to the microfluidic encapsulation unit. Alternatively, the liquid can also be transferred through the sample storage bag (61).
  • the tangential flow filter (31) performs a liquid exchange operation on the liposomes.
  • Step 4.1 Optionally, open the sampling head (65) to sample and detect the solution in the sample storage bag (61).
  • Step 5 Introduce the changed liposome solution into the preparation storage bag (71).
  • the liposomes are filled into the dispensing bottle through the filling pump tube (74) and the filling needle (75).

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Abstract

The present application relates to a system for preparing mRNA liposomes and use thereof. The system comprises a liquid preparation unit, an encapsulation unit, a liquid exchange unit, and a formulation unit according to the order in which they are connected. The system is a fully closed system. Using the system of the present application to produce mRNA liposomes can effectively avoid contamination and cross-contamination, reduce the frequency of sterilizing filtration, reduce the influence of the environment, equipment, personnel and other external factors on cell products, increase the yield, and improve the stability of products.

Description

一种制备mRNA脂质体的系统及其应用A system for preparing mRNA liposomes and its application 技术领域Technical field
本申请属于脂质体工艺领域,具体涉及一种制备mRNA脂质体的系统及其应用This application belongs to the field of liposome technology, and specifically relates to a system for preparing mRNA liposomes and its application.
背景技术Background technique
mRNA技术产品是基于mRNA指导蛋白合成的“中心法则”,在体外设计合成含有编码特定抗原的mRNA序列,经过序列优化、化学修饰和纯化等加工,采用不同方式递送至人体细胞,利用机体细胞翻译产生蛋白、诱导免疫应答、补充机体蛋白、调节免疫等作用,从而预防或治疗疾病。其应用领域广泛,主要用于如传染病疫苗的制备、肿瘤免疫治疗、单抗药物替代以及其他蛋白类药物替代等。目前进展最快、应用最多的是感染性疾病的预防性疫苗,以辉瑞所生产的BNT162b2为代表的mRNA疫苗在COVID-19的应用中大放异彩。mRNA technology products are based on the "central dogma" of mRNA guiding protein synthesis. They are designed and synthesized in vitro containing mRNA sequences encoding specific antigens. After sequence optimization, chemical modification and purification, they are delivered to human cells in different ways and are translated by the body's cells. Produce proteins, induce immune responses, supplement body proteins, regulate immunity, etc., thereby preventing or treating diseases. It has a wide range of applications, including the preparation of infectious disease vaccines, tumor immunotherapy, monoclonal antibody drug substitution, and other protein drug substitution. At present, the fastest-growing and most widely used vaccines are preventive vaccines for infectious diseases. The mRNA vaccine represented by BNT162b2 produced by Pfizer has shined in the application of COVID-19.
目前mRNA药品的生产中多有待改进之处。例如1)由于mRNA药品会回输至患者体内,为注射剂级别,按药典四部,对无菌控制级别要求极高,因此它的制备过程对环境、人员、设备的无菌控制要求非常高;2)常规的生产工艺同时生产不同样品时容易通过设备、环境、人员产生交叉污染,由此导致无法实现产品的多品种共线生产,而基因治疗产品生产本身就具有规模小、质量要求高、需求多产品共线生产等特点;3)mRNA脂质体生产工艺,主要通过增加除菌过滤工序来降低微生物负载,但除菌过滤会严重影响产品的回收率;4)mRNA脂质体生产阶段需要使用高浓度的乙醇溶液,生产过程中存在安全隐患等。因此市场上亟需一套全封闭的生产工艺以保证产品的本身质量与效果并促进整个基因治疗行业的发展。There are many areas for improvement in the current production of mRNA drugs. For example: 1) Since the mRNA drug will be infused back into the patient, it is an injection grade. According to Pharmacopoeia IV, the level of sterility control is extremely high, so its preparation process requires very high sterility control of the environment, personnel, and equipment; 2 ) When the conventional production process produces different samples at the same time, it is easy to cause cross-contamination through equipment, environment, and personnel, which makes it impossible to achieve multi-variety collinear production of products. The production of gene therapy products itself has small scale, high quality requirements, and demand. Features such as multi-product collinear production; 3) The production process of mRNA liposomes mainly reduces the microbial load by adding sterilization and filtration processes, but sterilization and filtration will seriously affect the recovery rate of the product; 4) The production stage of mRNA liposomes requires The use of high-concentration ethanol solutions may cause safety hazards during the production process. Therefore, there is an urgent need in the market for a fully enclosed production process to ensure the quality and effectiveness of the product and promote the development of the entire gene therapy industry.
发明内容Contents of the invention
本申请的目的在于提供一种制备mRNA脂质体的系统及其应用。使用本申请的系统进行mRNA脂质体的制备时,原料、中间产物以及终产物所流经的管路均为全封闭状态,能够有效避免污染与交叉污染,减少除菌过滤的次数,降低环境、设备、人员及以及其他外界因素对细胞产品造成的影响,提高产品的质量和稳定性。The purpose of this application is to provide a system for preparing mRNA liposomes and its application. When using the system of this application to prepare mRNA liposomes, the pipelines through which the raw materials, intermediate products and final products flow are fully closed, which can effectively avoid contamination and cross-contamination, reduce the number of sterilization filtrations, and reduce the environmental impact. , equipment, personnel and other external factors on cell products, and improve the quality and stability of the products.
在一个方面,本申请提供了一种制备mRNA脂质体的系统,所述系统按照连接顺序依 次包含配液单元、包封单元、换液单元以及制剂单元;In one aspect, the present application provides a system for preparing mRNA liposomes, which system follows the connection sequence. It includes liquid preparation unit, encapsulation unit, liquid replacement unit and preparation unit;
所述系统为全封闭系统。The system is a fully closed system.
本申请中的所述“单元”可以是一个仪器或者设备,或者能够完成某项工作的一组仪器或者设备的集合。这些不同的单元可以构成一个具有特定功能的系统。The "unit" in this application may be an instrument or equipment, or a set of instruments or equipment capable of completing a certain work. These different units can form a system with specific functions.
如本领域已知,“mRNA脂质体”,又被称为“mRNA-脂质体复合物”、“mRNA-脂质纳米复合物”、“mRNA-脂质体纳米复合物”、“脂质体-mRNA复合物”等,是一种采用包括但不限于薄膜水化法、挤出法、均质法、微流控等方式制备得到的脂质纳米颗粒(Lipid nanoparticle,LNP)。关于所涉及的脂质的种类,LNP的表面主要是中性脂质和PEG化脂质以及部分可电离的阳离子脂质和胆固醇;在核心内部,存在可电离的阳离子脂质、胆固醇。As known in the art, "mRNA liposomes" are also known as "mRNA-liposome complexes", "mRNA-lipid nanocomplexes", "mRNA-liposome nanocomplexes", "lipid nanocomplexes" "Plastid-mRNA complex", etc., is a lipid nanoparticle (Lipid nanoparticle, LNP) prepared by methods including but not limited to film hydration method, extrusion method, homogenization method, microfluidics, etc. Regarding the types of lipids involved, the surface of LNP is mainly neutral lipids and PEGylated lipids as well as partially ionizable cationic lipids and cholesterol; inside the core, ionizable cationic lipids and cholesterol are present.
如本文中所用,术语“信使RNA(mRNA)”是指编码至少一种多肽的多核苷酸。本文所用的mRNA包括修饰的和未修饰的RNA。mRNA可以含有一个或多个编码区和非编码区。本发明可以用于包封任何mRNA。As used herein, the term "messenger RNA (mRNA)" refers to a polynucleotide encoding at least one polypeptide. As used herein, mRNA includes modified and unmodified RNA. An mRNA may contain one or more coding and non-coding regions. The present invention can be used to encapsulate any mRNA.
本申请中的所述配液单元可为本领域常规的配液罐,可选择地,其带有常规搅拌装置或者磁力搅拌装置。本申请中配液单元的功能包括但不限于将合适浓度的mRNA缓冲液溶解于偏酸性的溶液以形成水相,将脂质溶解于乙醇形成有机相。所述配液单元可按照本领域的常规制备方法制备所述水相和所述有机相,使其具备足以形成mRNA脂质体的成分特性。The liquid preparation unit in this application can be a conventional liquid preparation tank in this field, optionally, it is equipped with a conventional stirring device or a magnetic stirring device. The functions of the liquid preparation unit in this application include but are not limited to dissolving an appropriate concentration of mRNA buffer in a slightly acidic solution to form an aqueous phase, and dissolving lipids in ethanol to form an organic phase. The liquid preparation unit can prepare the aqueous phase and the organic phase according to conventional preparation methods in the art, so that they have sufficient composition characteristics to form mRNA liposomes.
mRNA原液的制备可为本领域常规,例如可包含体外转录、转录后修饰、酶处理、层析纯化、浓缩换液、原液配制等一系列步骤。进行该系列步骤所使用的仪器/设备均可为本领域常规,其构成所述用于制备mRNA原液的单元。The preparation of the mRNA stock solution may be routine in the art, and may include, for example, a series of steps such as in vitro transcription, post-transcriptional modification, enzyme treatment, chromatography purification, concentration and medium replacement, and stock solution preparation. The instruments/equipment used to perform this series of steps can all be conventional in the art, and they constitute the unit for preparing the mRNA stock solution.
可选择地,所述配液单元还具备对mRNA原液进行复融的功能。用于复融的仪器/设备可为本领域常规。可以使用各种方法来制备适合用于本发明的mRNA溶液。在一些实施方案中,可以将mRNA直接溶解在本文所述的缓冲溶液中。在一些实施方案中,可以通过与有机相混合以进行包封之前将mRNA原液与缓冲溶液混合来产生mRNA溶液。Optionally, the liquid preparation unit also has the function of remelting the original mRNA solution. Instruments/equipment used for refusion may be routine in the art. Various methods can be used to prepare mRNA solutions suitable for use in the present invention. In some embodiments, the mRNA can be dissolved directly in the buffer solutions described herein. In some embodiments, the mRNA solution can be produced by mixing the mRNA stock solution with a buffer solution before mixing with the organic phase for encapsulation.
在一些实施方案中,配液单元还可以将mRNA原液与缓冲溶液混合。In some embodiments, the liquid preparation unit can also mix the mRNA stock solution and the buffer solution.
有机相含有适合于形成用于包封mRNA的脂质纳米颗粒的脂质混合物。在一些实施方案中,合适的有机相是基于乙醇的。例如,合适的有机相可以含有溶解在纯乙醇(即,100%乙醇)中的所需脂质的混合物。在另一个实施方案中,合适的有机相是基于异丙醇的。在另 一个实施方案中,合适的有机相是基于二甲基亚砜的。在另一个实施方案中,合适的有机相是合适溶剂(包括但不限于乙醇、异丙醇和二甲基亚砜)的混合物。The organic phase contains a mixture of lipids suitable for forming lipid nanoparticles for encapsulating mRNA. In some embodiments, a suitable organic phase is ethanol-based. For example, a suitable organic phase may contain a mixture of desired lipids dissolved in pure ethanol (ie, 100% ethanol). In another embodiment, a suitable organic phase is isopropyl alcohol based. in another In one embodiment, a suitable organic phase is based on dimethyl sulfoxide. In another embodiment, a suitable organic phase is a mixture of suitable solvents including, but not limited to, ethanol, isopropanol, and dimethyl sulfoxide.
在一些实施方案中,所述有机相包含一种或多种阳离子脂质、一种或多种辅助脂质和一种或多种PEG修饰的脂质。在一些实施方案中,所述有机相还包含一种或多种基于胆固醇的脂质。在一些实施方案中,所述一种或多种基于胆固醇的脂质是胆固醇和/或PEG化的胆固醇。在一些实施方案中,所述有机相包含预先形成的脂质纳米颗粒。在一些实施方案中,所述有机相是预先形成的脂质纳米颗粒的悬浮液。In some embodiments, the organic phase includes one or more cationic lipids, one or more helper lipids, and one or more PEG-modified lipids. In some embodiments, the organic phase further includes one or more cholesterol-based lipids. In some embodiments, the one or more cholesterol-based lipids are cholesterol and/or PEGylated cholesterol. In some embodiments, the organic phase includes preformed lipid nanoparticles. In some embodiments, the organic phase is a suspension of preformed lipid nanoparticles.
合适的有机相可以含有各种浓度的所需脂质的混合物。例如,合适的有机相可以含有总浓度等于或大于约0.1mg/ml、1.0mg/ml、10mg/ml或100mg/ml的所期望的脂质的混合物。A suitable organic phase may contain a mixture of various concentrations of the desired lipids. For example, a suitable organic phase may contain a mixture of the desired lipids at a total concentration equal to or greater than about 0.1 mg/ml, 1.0 mg/ml, 10 mg/ml, or 100 mg/ml.
可选择地,所述配液单元还具备控制所述水相和有机相的比率的功能。任何所需脂质可以任何适合于包封mRNA的比率混合。在一些实施方案中,合适的有机相含有所需脂质的混合物,所述所需脂质包括阳离子脂质、辅助脂质(例如,非阳离子脂质和/或胆固醇脂质)和/或PEG化的脂质。在一些实施方案中,合适的有机相含有所需脂质的混合物,所述所需脂质包括一种或多种阳离子脂质、一种或多种辅助脂质(例如,非阳离子脂质和/或胆固醇脂质)和一种或多种PEG化的脂质。Optionally, the liquid preparation unit also has the function of controlling the ratio of the aqueous phase and the organic phase. Any desired lipids can be mixed in any ratio suitable for encapsulating mRNA. In some embodiments, a suitable organic phase contains a mixture of desired lipids including cationic lipids, accessory lipids (e.g., non-cationic lipids and/or cholesterol lipids), and/or PEG oxidized lipids. In some embodiments, a suitable organic phase contains a mixture of desired lipids including one or more cationic lipids, one or more accessory lipids (e.g., non-cationic lipids and /or cholesterol lipids) and one or more PEGylated lipids.
本申请中的所述脂质可为本领域常规,包括但不限于阳离子脂质(如ALC-0315,CAS:2036272-55-4)、胆固醇、辅助型脂质(如DOPE)以及聚乙二醇化磷脂(如PEG2000-DMG)等。其中:所述阳离子脂质的作用包括但不限于,与带负电的mRNA结合,高效包载mRNA药物。所述胆固醇的作用包括但不限于,通过调节膜的流动性稳定mRNA脂质体的结构、提高mRNA脂质体的稳定性。所述辅助型脂质的作用包括但不限于,稳定mRNA脂质体,提高递送mRNA的效率。所述聚乙二醇化磷脂的作用包括但不限于,提高mRNA脂质体的稳定性,减少其与血浆蛋白的结合,延长其在体内的循环时间。The lipids in this application can be conventional in the art, including but not limited to cationic lipids (such as ALC-0315, CAS: 2036272-55-4), cholesterol, auxiliary lipids (such as DOPE), and polyethylene glycol. Alcoholized phospholipids (such as PEG2000-DMG), etc. Among them: the functions of the cationic lipid include, but are not limited to, binding to negatively charged mRNA and efficiently entrapping mRNA drugs. The functions of cholesterol include, but are not limited to, stabilizing the structure of the mRNA liposomes and improving the stability of the mRNA liposomes by regulating the fluidity of the membrane. The functions of the auxiliary lipid include, but are not limited to, stabilizing mRNA liposomes and improving the efficiency of delivering mRNA. The functions of the PEGylated phospholipids include, but are not limited to, improving the stability of mRNA liposomes, reducing their binding to plasma proteins, and prolonging their circulation time in the body.
根据各种实施方案,包含脂质纳米颗粒的阳离子脂质、辅助型脂质、基于胆固醇的脂质和/或PEG修饰的脂质的选择,以及这些脂质与彼此的相对摩尔比基于所选择的脂质的特征、预期靶细胞的性质、待递送的mRNA的特征。其他考虑因素包括例如,烷基链的饱和度以及所选脂质的大小、电荷、pH、pKa、融合性和毒性。因此,可相应地调节摩尔比。According to various embodiments, the selection of cationic lipids, helper lipids, cholesterol-based lipids, and/or PEG-modified lipids comprising lipid nanoparticles, and the relative molar ratios of these lipids to each other are based on the selection Characteristics of the lipids, the nature of the intended target cells, and the characteristics of the mRNA to be delivered. Other considerations include, for example, the saturation of the alkyl chain and the size, charge, pH, pKa, fusogenicity, and toxicity of the selected lipid. Therefore, the molar ratio can be adjusted accordingly.
在某些实施方式中,本申请中的所述配液单元为防爆配液单元。该防爆配液单元的功 能包括但不限于可有效避免在有机相制备过程中,使用高浓度乙醇溶液所带来的安全隐患。所述的防爆配液单元可为本领域中常规,例如不锈钢防爆配液灌。In some embodiments, the liquid preparation unit in this application is an explosion-proof liquid preparation unit. The function of the explosion-proof liquid dispensing unit This can include, but is not limited to, effectively avoiding safety hazards caused by using high-concentration ethanol solutions during the preparation of the organic phase. The explosion-proof liquid dispensing unit may be conventional in the field, such as a stainless steel explosion-proof liquid dispensing tank.
本申请中,所述包封单元的功能包括但不限于控制两相溶液的注入温度、压力、流量以及比率等,并通过薄膜水化法、挤出法、均质法、超声波、剪切或者微流控混合等LNP制备方法来制备mRNA脂质体。In this application, the functions of the encapsulation unit include but are not limited to controlling the injection temperature, pressure, flow rate and ratio of the two-phase solution, etc., and use the film hydration method, extrusion method, homogenization method, ultrasonic wave, shearing or Microfluidic mixing and other LNP preparation methods are used to prepare mRNA liposomes.
在某些实施方式中,本申请中的所述包封单元为微流控包封单元,其通过微流控混合的方法制备mRNA脂质体。所述微流控包封单元的一个运行示例为,有机相与水相通过喷射碰撞对冲混合,同时有机相中的乙醇被稀释,溶液pH变化,脂质体析出形成脂质纳米颗粒并与mRNA形成包封复合物。In certain embodiments, the encapsulation unit in this application is a microfluidic encapsulation unit, which prepares mRNA liposomes through a microfluidic mixing method. An example of the operation of the microfluidic encapsulation unit is that the organic phase and the aqueous phase are mixed by jet collision. At the same time, the ethanol in the organic phase is diluted, the pH of the solution changes, and the liposomes separate out to form lipid nanoparticles and interact with the mRNA. Formation of encapsulated complexes.
所述微流控包封单元的结构可为本领域常规,例如包含高压泵以及腔体,所述高压泵用于使所述水相和有机相形成两股射流,在所述腔体中进行对冲。在某些实施方式中,通过所述微流控包封单元制备mRNA脂质体过程中液体对冲的流速是可控制的。在某些实施方式中,可以控制微流控芯片中储集器、导管和/或接头中的至少一者的直径以实现所期望的流速和所得的混合性质。导管的直径越大,液体通过导管的流量越大。在某些实施方式中,在微流控芯片中采取限流设置以实现所期望的流速和所得的混合性质。The structure of the microfluidic encapsulation unit can be conventional in the art, for example, it includes a high-pressure pump and a cavity. The high-pressure pump is used to form two jets of the aqueous phase and the organic phase, and the process is carried out in the cavity. Hedge. In certain embodiments, the flow rate of the liquid buffer during the preparation of mRNA liposomes through the microfluidic encapsulation unit is controllable. In certain embodiments, the diameter of at least one of the reservoirs, conduits, and/or connectors in the microfluidic chip can be controlled to achieve desired flow rates and resulting mixing properties. The larger the diameter of the conduit, the greater the flow of liquid through the conduit. In certain embodiments, flow limiting settings are employed in the microfluidic chip to achieve the desired flow rate and resulting mixing properties.
在某些实施方式中,本申请中所述的微流控包封单元制备mRNA脂质体的过程是无菌的。在某些实施方式中,本申请中所述的微流控包封单元不是在无菌环境下的。在某些实施方式中,所述微流控包封单元允许mRNA在脂质中的可重复的包封。在某些实施方式中,所述微流控包封单元允许脂质纳米颗粒(LNP)的可重复的产生。In certain embodiments, the process of preparing mRNA liposomes by the microfluidic encapsulation unit described in this application is sterile. In certain embodiments, the microfluidic encapsulation units described herein are not in a sterile environment. In certain embodiments, the microfluidic encapsulation unit allows reproducible encapsulation of mRNA in lipids. In certain embodiments, the microfluidic encapsulation unit allows reproducible production of lipid nanoparticles (LNPs).
所述微流控包封单元的生产厂家可选自Genizer、Precision NanoSystems(PNI)、PreciGenome、Dolomite Microfluidics、迈安纳(上海)仪器科技有限公司以及苏州艾特森制药设备有限公司等。The manufacturers of the microfluidic encapsulation unit can be selected from Genizer, Precision NanoSystems (PNI), PreciGenome, Dolomite Microfluidics, Myanna (Shanghai) Instrument Technology Co., Ltd., and Suzhou Aitson Pharmaceutical Equipment Co., Ltd., etc.
通过包封单元所获得的产物中,除mRNA脂质体外还存在有未利用的mRNA或其片段、未利用的脂质、乙醇以及可能存在的微生物等杂质。使用本申请中的换液单元对上述杂质进行移除以获得纯化的mRNA脂质体,并可依据对mRNA脂质体的功能或配方需求进行制剂配液,例如添加利于产品的长期稳定储存和药效发挥的辅料成分(如蔗糖)等。In the product obtained by the encapsulation unit, in addition to the mRNA liposome, there are also impurities such as unused mRNA or its fragments, unused lipids, ethanol, and possible microorganisms. The above-mentioned impurities are removed using the liquid exchange unit in this application to obtain purified mRNA liposomes, and preparations can be made according to the function or formula requirements of the mRNA liposomes, for example, adding ingredients to facilitate long-term stable storage of the product and Excipient ingredients (such as sucrose) that exert the medicinal effect.
在某些实施方式中,本申请中的所述换液单元为切向流过滤换液单元。切向流过滤(Tangential Flow Filtration,TFF)又称为错流过滤(Cross Flow Filtration),是指液体流动 方向于过滤方向呈垂直方向的过滤形式,通过压力驱动,根据分子尺寸进行膜分离。本申请中所述切向流过滤单元中膜的截留孔径可依据所制备mRNA脂质体的粒径而定。In some embodiments, the liquid exchange unit in this application is a tangential flow filtration liquid exchange unit. Tangential Flow Filtration (TFF), also known as Cross Flow Filtration, refers to the flow of liquid The filtration form is perpendicular to the filtration direction. It is driven by pressure and performs membrane separation based on molecular size. The cutoff pore size of the membrane in the tangential flow filtration unit described in this application can be determined based on the particle size of the prepared mRNA liposomes.
在TFF中,通过切向流原理完成浓缩和换液。In TFF, concentration and liquid replacement are accomplished through the tangential flow principle.
切向流过滤的主要优点是改为沿着过滤器的表面运送在传统“死端”过滤期间可在过滤器内聚集并阻塞过滤器的非渗透性渗余物或“滤饼”。该优点使得切向流过滤尤其适于大规模纯化mRNA脂质体。The main advantage of tangential flow filtration is that the non-permeable retentate or "filter cake" that can collect within the filter and clog it during traditional "dead-end" filtration is instead transported along the surface of the filter. This advantage makes tangential flow filtration particularly suitable for large-scale purification of mRNA liposomes.
在典型TFF过程中重要的至少三个过程变量:跨膜压差、进料速率和渗透物的流速。跨膜压差是推动流体带着渗透性分子一起通过过滤器的力。进料速率(也称为错流速度)是溶液流过进料通道并穿过过滤器的速率。进料速率决定了清除可能以其它方式填塞或污损过滤器并从而限制滤液流速的分子的力。渗透物的流速是从体系中去除渗透物的速率。对于恒定进料速率而言,增加渗透物流速可增加穿过过滤器的压力,导致过滤速率提高,同时还可能增加过滤器堵塞或污损的风险。Michaels等,"Tangential Flow Filtration"in Separations Technology,Pharmaceutical and Biote chnology Applications(W.P.Olson编,Interpharm Press,Inc.,Buffalo Grove,1995)中描述了用于TFF的原理、理论和装置。还可参见美国专利第5,256,294和5,490,937号对高性能切向流过滤(HP-TFF)的描述。At least three process variables are important in a typical TFF process: transmembrane pressure differential, feed rate, and permeate flow rate. The transmembrane pressure differential is the force that pushes fluid through the filter, carrying permeable molecules with it. Feed rate (also called cross-flow rate) is the rate at which solution flows through the feed channel and through the filter. The feed rate determines the force that removes molecules that might otherwise clog or foul the filter and thereby limit the filtrate flow rate. The permeate flow rate is the rate at which permeate is removed from the system. For a constant feed rate, increasing the permeate flow rate increases the pressure across the filter, resulting in an increase in filtration rate, and may also increase the risk of filter clogging or fouling. The principles, theory, and apparatus for TFF are described in Michaels et al., "Tangential Flow Filtration" in Separations Technology, Pharmaceutical and Biotechnology Applications (W.P. Olson, ed., Interpharm Press, Inc., Buffalo Grove, 1995). See also the description of high performance tangential flow filtration (HP-TFF) in US Pat. Nos. 5,256,294 and 5,490,937.
在某些实施方式中,本申请中所述全封闭可通过一次性封闭工艺实现。例如,使用无菌接头/无菌阻断器连接/断开不同的单元。其中,根据所连接单元的不同,所述无菌接头可为无菌连接器或者无菌接管机;根据所断开的连接单元的不同,所述阻断器可为无菌断开器或者无菌封管机。In some embodiments, the total sealing described in this application can be achieved through a one-time sealing process. For example, use sterile connectors/sterile interrupters to connect/disconnect different units. Wherein, depending on the connected unit, the aseptic connector can be a sterile connector or a sterile takeover machine; depending on the disconnected connection unit, the blocker can be a sterile disconnector or a sterile disconnector. Bacteria sealing tube machine.
本发明的另一个优势是合理地设计了无菌区面积,特别是核心无菌生产区域面积,减少无菌保障成本。在某些实施方式中,制剂单元处于C级区。在某些实施方式中,换液单元以及制剂单元处于C级区。在某些实施方式中,换液单元以及制剂单元处于C级区。Another advantage of the present invention is that the area of the sterile area, especially the core sterile production area, is reasonably designed to reduce the cost of sterility assurance. In certain embodiments, the formulation unit is in the Class C zone. In some embodiments, the fluid exchange unit and the preparation unit are in the Class C zone. In some embodiments, the fluid exchange unit and the preparation unit are in the Class C zone.
在某些实施方式中,所述系统按照其连接顺序依次为防爆配液单元、无菌连接器/无菌断开器、微流控包封单元、无菌接管机/无菌封管机、TFF换液单元、无菌接管机/无菌封管机以及脂质体制剂单元。本申请中所述地各单元的连接顺序优选与规模生产中的步骤一致。In some embodiments, the system, in order of connection, is an explosion-proof liquid preparation unit, a sterile connector/sterile disconnector, a microfluidic encapsulation unit, a sterile take-over machine/a sterile tube sealing machine, TFF liquid changing unit, sterile tube taking machine/sterile sealing machine and liposome preparation unit. The connection sequence of each unit described in this application is preferably consistent with the steps in large-scale production.
在某些实施方式中,所述配液单元和所述包封单元之间的连接通过无菌连接器实现。In some embodiments, the connection between the liquid preparation unit and the encapsulation unit is achieved through a sterile connector.
在某些实施方式中,所述配液单元和所述包封单元之间的断开通过无菌断开器实现。 In some embodiments, the disconnection between the dispensing unit and the encapsulating unit is achieved by a sterile disconnect.
在某些实施方式中,所述流体混合包封单元和所述换液单元之间的连接通过无菌接管机实现。In some embodiments, the connection between the fluid mixing and encapsulation unit and the liquid exchange unit is achieved through a sterile pipe machine.
在某些实施方式中,所述流体混合包封单元和所述换液单元之间的断开通过无菌封管机实现。In some embodiments, the disconnection between the fluid mixing and encapsulation unit and the fluid exchange unit is accomplished by a sterile sealing machine.
在某些实施方式中,所述换液单元和所述制剂单元之间的连接通过无菌接管机实现。In some embodiments, the connection between the liquid changing unit and the preparation unit is realized through a sterile pipe machine.
在某些实施方式中,所述换液单元和所述制剂单元之间的断开通过无菌封管机实现。In some embodiments, the disconnection between the liquid exchange unit and the preparation unit is achieved by a sterile sealing machine.
本申请中所述接头和阻断器的使用能够有效地连接不同的单元,使mRNA脂质体的制备在本领域中首次实现mRNA脂质体一体化生产工艺,克服了不同的供应商质检的设备缺乏设备之间的整合和连接的缺陷。The use of linkers and blockers described in this application can effectively connect different units, enabling the preparation of mRNA liposomes to realize an integrated production process of mRNA liposomes for the first time in this field, overcoming the quality inspection of different suppliers. The device lacks integration and connection defects between devices.
如本文所述的无菌连接器/无菌断开器允许快速轻松完成无菌连接和断开,即使在非无菌环境也能如此。在某些实施方式中,所述无菌连接器/无菌断开器可以作为除菌滤器对溶液进行过滤。在某些实施方式中,所述系统在无菌连接器/无菌断开器之后不包括其他除菌滤器。Sterile connectors/sterile disconnectors as described in this article allow for quick and easy sterile connection and disconnection, even in non-sterile environments. In certain embodiments, the sterile connector/disconnector can act as a sterile filter to filter the solution. In certain embodiments, the system does not include additional sterile filters after the sterile connector/sterile disconnector.
在某些实施方式中,防爆配液单元之后设置有过滤器作为除菌滤器。在某些实施方式中,防爆配液单元之后设置0.22μm滤芯过滤去除溶液内残留的微生物,达到无菌级别为SAL=10E-6。在某些实施方式中,在所述系统中,连接在所述防爆配液单元之后的其他除菌滤器数量小于5个。在某些实施方式中,在所述系统中,连接在所述防爆配液单元之后的其他除菌滤器数量小于3个。在某些实施方式中,在所述系统中,连接在所述防爆配液单元之后的其他除菌滤器数量小于1个。In some embodiments, a filter is provided as a sterilizing filter after the explosion-proof liquid preparation unit. In some embodiments, a 0.22 μm filter element is installed after the explosion-proof liquid preparation unit to filter and remove residual microorganisms in the solution, and the sterility level is SAL=10E-6. In some embodiments, in the system, the number of other sterilizing filters connected after the explosion-proof liquid preparation unit is less than 5. In some embodiments, in the system, the number of other sterilizing filters connected after the explosion-proof liquid preparation unit is less than 3. In some embodiments, in the system, the number of other sterilizing filters connected after the explosion-proof liquid preparation unit is less than 1.
在某些实施方式中,在所述系统中的除菌滤器数量小于5个。在某些实施方式中,在所述系统中的除菌滤器数量小于4个。在某些实施方式中,在所述系统中的除菌滤器数量小于3个。在某些实施方式中,在所述系统中的除菌滤器数量小于2个。在某些实施方式中,在所述系统中的除菌滤器数量小于1个。In certain embodiments, the number of sterile filters in the system is less than 5. In certain embodiments, the number of sterile filters in the system is less than 4. In certain embodiments, the number of sterile filters in the system is less than 3. In certain embodiments, the number of sterile filters in the system is less than 2. In certain embodiments, the number of sterile filters in the system is less than 1.
可选择地,本申请中的所述系统在所述配液单元的上游还包括用于制备质粒DNA原液的单元和用于制备mRNA原液的单元。该类制备原液的单元之间以及其与配液单元的连接/断开通过无菌连接器/无菌断开器实现。Optionally, the system in this application further includes a unit for preparing plasmid DNA stock solution and a unit for preparing mRNA stock solution upstream of the liquid preparation unit. The connection/disconnection between such units for preparing raw solutions and between them and the liquid dispensing unit is achieved through sterile connectors/sterile disconnectors.
质粒DNA原液的制备可为本领域常规,例如可包含发酵培养、收获澄清、精制纯化、线性化以及过滤分装等步骤。进行该系列步骤所使用的仪器/设备均可为本领域常规,例如 细菌培养发酵罐、CO2培养箱、离心机以及用于切向流过滤或者深层过滤的设备等,其构成所述用于制备质粒DNA原液的单元。The preparation of the plasmid DNA stock solution may be routine in the art, and may include steps such as fermentation culture, harvesting and clarification, refining and purification, linearization, and filtration and aliquots. The instruments/equipment used to perform this series of steps can all be conventional in the art, for example Bacterial culture fermentation tanks, CO 2 incubators, centrifuges, and equipment for tangential flow filtration or depth filtration, etc., constitute the unit for preparing plasmid DNA stock solution.
可选择地,本申请中的所述系统在所述制剂单元的下游还包含使用制备得到的mRNA脂质体制备细胞疗法相关产品的单元。Optionally, the system in the present application further includes a unit downstream of the preparation unit for preparing cell therapy-related products using the prepared mRNA liposomes.
在另一个方面,本申请提供了一种制备mRNA脂质体的方法,其包括使用如第一方面所述的系统进行制备。In another aspect, the present application provides a method for preparing mRNA liposomes, which includes preparing using a system as described in the first aspect.
采用所述系统制备mRNA脂质体时,可依次进行如下操作:防爆对接、流体对接、样品取样、缓冲液保存及转移以及样本液保存及转移。When using the system to prepare mRNA liposomes, the following operations can be performed in sequence: explosion-proof docking, fluid docking, sample sampling, buffer storage and transfer, and sample solution storage and transfer.
若无特别说明,本申请中对各单元的操作均可为本领域中的成熟工艺,例如使用配液单元进行两相的配制、使用包封单元对mRNA进行包封。Unless otherwise specified, the operation of each unit in this application can be a mature process in the field, such as using a liquid preparation unit to prepare two phases and using an encapsulation unit to encapsulate mRNA.
本申请所述系统为全封闭系统,使用过程中可采用一次性封闭工艺,有效避免污染与交叉污染,减少除菌过滤的次数,降低环境、设备、人员及以及其他外界因素对细胞产品造成的影响,增加产量并提升产品的稳定性。与现有技术相比,本申请所述系统合理地将各单元分为了防爆区和C级区。在某些实施方式中,防爆配液单元和包封单元构成防爆区,换液单元以及制剂单元构成C级区。本申请的系统中含有防爆配液单元时能够提供防爆生产环境,有效防爆。而纯化、制剂、包装工序在C级或更高级别的洁净区内进行,使得纯化、制剂、包装过程中没有微生物污染。防爆区和C级区之间采用无菌连接/断开,整个工艺流程中无需对C级区的设备可进行多次重复灭菌处理,极大简化了生产工艺。The system described in this application is a fully closed system. A one-time closed process can be used during use to effectively avoid contamination and cross-contamination, reduce the number of sterilization filtrations, and reduce the impact of the environment, equipment, personnel, and other external factors on cell products. impact, increase production and improve product stability. Compared with the existing technology, the system described in this application reasonably divides each unit into an explosion-proof area and a Class C area. In some embodiments, the explosion-proof liquid preparation unit and the encapsulation unit constitute an explosion-proof area, and the liquid replacement unit and the preparation unit constitute a Class C area. When the system of this application contains an explosion-proof liquid dispensing unit, it can provide an explosion-proof production environment and effectively prevent explosions. The purification, preparation, and packaging processes are carried out in clean areas of Class C or higher, so that there is no microbial contamination during the purification, preparation, and packaging processes. Aseptic connection/disconnection is adopted between the explosion-proof area and the C-level area. The equipment in the C-level area does not need to be sterilized multiple times during the entire process, which greatly simplifies the production process.
在某些实施方式中,在所述防爆对接,和/或流体对接步骤之后不需要对C级区的设备进行灭菌处理。在某些实施方式中,在每次间歇生产过程中对所述C级区的设备的灭菌处理次数少于10次。在某些实施方式中,在每次间歇生产过程中对所述C级区的设备的灭菌处理次数少于5次。在某些实施方式中,在每次间歇生产过程中对所述C级区的设备的灭菌处理次数少于4次。在某些实施方式中,在每次间歇生产过程中对所述C级区的设备的灭菌处理次数少于3次。在某些实施方式中,在每次间歇生产过程中对所述C级区的设备的灭菌处理次数少于2次。在某些实施方式中,在每次间歇生产过程中对所述C级区的设备的灭菌处理次数少于1次。In some embodiments, the equipment in the Class C area does not need to be sterilized after the explosion-proof docking and/or fluid docking steps. In some embodiments, the equipment in the Level C zone is sterilized less than 10 times during each intermittent production process. In some embodiments, the equipment in the Level C zone is sterilized less than 5 times during each intermittent production process. In some embodiments, the equipment in the Level C zone is sterilized less than 4 times during each intermittent production process. In some embodiments, the equipment in the Level C zone is sterilized less than three times during each intermittent production process. In some embodiments, the equipment in the Level C zone is sterilized less than twice during each intermittent production process. In some embodiments, the equipment in the Level C zone is sterilized less than once during each intermittent production process.
在某些实施方式中,如本文所描述的系统可以用于连续生产工艺。在某些实施方式中, 在连续生产过程中对所述C级区的设备的灭菌处理频率少于10次每天。在某些实施方式中,在连续生产过程中对所述C级区的设备的灭菌处理次每天数少于5次每天。在某些实施方式中,在连续生产过程中对所述C级区的设备的灭菌处理次每天数少于4次每天。在某些实施方式中,在连续生产过程中对所述C级区的设备的灭菌处理次每天数少于3次每天。在某些实施方式中,在连续生产过程中对所述C级区的设备的灭菌处理次每天数少于2次每天。在某些实施方式中,在连续生产过程中对所述C级区的设备的灭菌处理次每天数少于1次每天。In certain embodiments, systems as described herein can be used in continuous production processes. In some embodiments, The frequency of sterilization treatment of equipment in the Class C area during continuous production is less than 10 times per day. In some embodiments, the equipment in the Level C zone is sterilized less than 5 times per day during the continuous production process. In some embodiments, the equipment in the Level C zone is sterilized less than 4 times per day during the continuous production process. In some embodiments, the equipment in the Level C zone is sterilized less than three times per day during the continuous production process. In some embodiments, the equipment in the Level C zone is sterilized less than 2 times per day during the continuous production process. In some embodiments, the equipment in the Level C zone is sterilized less than once per day during the continuous production process.
本申请所提供的用于制备mRNA脂质体的系统为mRNA脂质体一体化设备的合作开发提供了新的思路。The system for preparing mRNA liposomes provided in this application provides new ideas for the cooperative development of integrated equipment for mRNA liposomes.
以上为本申请的概述,可能有简化、概括和省略细节的情况,因此本领域的技术人员应该认识到,该部分仅是示例说明性的,而非旨在以任何方式限定本申请范围。本概述部分既非旨在确定所要求保护主题的关键特征或必要特征,也非旨在用作为确定所要求保护主题的范围的辅助手段。The above is an overview of the present application, and there may be situations where simplifications, generalizations, and details are omitted. Therefore, those skilled in the art should realize that this part is only illustrative and is not intended to limit the scope of the present application in any way. This Summary is neither intended to identify key features or essential features of the claimed subject matter, nor is it intended to be used as an aid in determining the scope of the claimed subject matter.
通过下面说明书和所附的权利要求书并与附图结合,将会更加充分地清楚理解本申请内容的上述和其他特征。可以理解,这些附图仅描绘了本申请内容的若干实施方式,因此不应认为是对本申请内容范围的限定。通过参考附图,本申请的内容将会得到更加明确和详细的说明。The above and other features of the present application will be more fully understood from the following description and appended claims, taken in conjunction with the accompanying drawings. It will be understood that these drawings only depict several embodiments of the present application and therefore should not be considered as limiting the scope of the present application. By referring to the accompanying drawings, the contents of this application will be explained more clearly and in detail.
附图说明Description of drawings
图1示出了本申请实施例1中用于制备mRNA脂质体的系统。Figure 1 shows the system used to prepare mRNA liposomes in Example 1 of the present application.
图2示出了将待液体从液体防爆配液单元转移至包封单元的储液袋。Figure 2 shows a liquid storage bag that transfers liquid to be liquid from the liquid explosion-proof dispensing unit to the encapsulation unit.
图3示出了TFF换液单元。Figure 3 shows the TFF fluid exchange unit.
图4示出了用于转移样品的样品储液袋。Figure 4 shows a sample storage bag used to transfer samples.
图5示出了用于转移制剂和灌装制剂的制剂储液袋。Figure 5 shows a formulation storage bag for transferring and filling formulations.
具体实施方式Detailed ways
详细描述、附图和权利要求书中描述的说明性实施方式并非旨在限定。在不偏离本申请的主题的精神或范围的情况下,可以采用其他实施方式,并且可以做出其他变化。可以理解,可以对本申请中一般性描述的、在附图中图解说明的本申请内容的各 个方面进行多种不同构成的配置、替换、组合、设计,而所有这些都明确地构成本申请内容的一部分。The illustrative embodiments described in the detailed description, drawings, and claims are not intended to be limiting. Other embodiments may be utilized, and other changes may be made, without departing from the spirit or scope of the subject matter of this application. It will be understood that various aspects of the subject matter generally described in this application and illustrated in the accompanying drawings may be A variety of configurations, substitutions, combinations, and designs can be made in various aspects, and all of these clearly form part of the content of this application.
实施例Example
为了可以更充分地理解本申请,示出了以下实施例。应当理解,这些实施例仅出于说明性目的,而不以任何方式解释为是限制性的。In order that the present application may be more fully understood, the following examples are set forth. It should be understood that these examples are for illustrative purposes only and are not to be construed as limiting in any way.
实施例1:用于制备mRNA脂质体的系统的构成Example 1: Composition of a system for preparing mRNA liposomes
系统主要由防爆配液单元(1)、微流控包封单元(2)、TFF换液单元(3)以及制剂单元(4)组成。其中,防爆配液单元和微流控包封单元构成防爆区,TFF换液单元以及制剂单元构成C级区(见图1)。The system mainly consists of an explosion-proof liquid preparation unit (1), a microfluidic encapsulation unit (2), a TFF liquid replacement unit (3) and a preparation unit (4). Among them, the explosion-proof liquid preparation unit and microfluidic encapsulation unit constitute the explosion-proof area, and the TFF liquid replacement unit and preparation unit constitute the C-level area (see Figure 1).
防爆配液单元(1)和微流控包封单元(2)之间采用无菌连接器/无菌断开器进行连接/断开。The explosion-proof liquid preparation unit (1) and the microfluidic encapsulation unit (2) are connected/disconnected using a sterile connector/sterile disconnector.
图2提供了将待包封液体从液体防爆配液单元转移至包封单元(2)的储液袋。液体(如mRNA溶液)从防爆配液单元(1)流经过滤器(57)和储液袋进液导管(52)流入储液袋(51)。过滤器(57)可以过滤配液单元中流入的液体。储液袋(51)配备有取样头(55)。取样头可以方便提取储液袋(51)的溶液。其中,储液袋进液导管(52)、储液袋出液导管(54)均可为热塑管,包含但不限于硅胶管、等。如有需要,热塑管可以用于无菌焊接,用于液体传输。储液袋出液导管(54)端口配有空气滤头(56)防止空气中污染物,特别是细菌的进入。储液袋进液导管(52)、储液袋出液导管(54)上安装有管夹(53)用以控制管路的开闭。Figure 2 provides a liquid storage bag that transfers the liquid to be encapsulated from the liquid explosion-proof dispensing unit to the encapsulation unit (2). Liquid (such as mRNA solution) flows from the explosion-proof liquid preparation unit (1) through the filter (57) and the liquid storage bag inlet conduit (52) into the liquid storage bag (51). The filter (57) can filter the liquid flowing into the dosing unit. The liquid storage bag (51) is equipped with a sampling head (55). The sampling head can conveniently extract the solution from the liquid storage bag (51). Among them, the liquid storage bag inlet conduit (52) and the liquid storage bag outlet conduit (54) can be thermoplastic tubes, including but not limited to silicone tube, and wait. If required, thermoplastic tubing can be used for aseptic welding for liquid transfer. The port of the liquid storage bag outlet conduit (54) is equipped with an air filter head (56) to prevent the entry of pollutants in the air, especially bacteria. Pipe clamps (53) are installed on the liquid storage bag liquid inlet conduit (52) and the liquid storage bag liquid outlet conduit (54) to control the opening and closing of the pipelines.
储液袋(51)中可以通过储液袋出液导管(54)与微流控包封单元(2)相连接。The liquid storage bag (51) can be connected to the microfluidic encapsulation unit (2) through the liquid storage bag outlet conduit (54).
微流控包封单元和TFF换液单元之间以及TFF换液单元和制剂单元之间采用无菌接管机/无菌封管机进行连接/断开。图3示出了TFF换液单元。其中进液导管(32)可与微流控包封单元(2)通过无菌接管机/无菌封管机进行连接/断开。其中回流液导管(33)可与制剂单元(3)通过无菌接管机/无菌封管机进行连接/断开。经微流控包封单元制备得到的mRNA脂质体经进液导管(32)流入切向流过滤器(31)。渗透液经渗透液导管(34)流入和流出切向流过滤器(31)从而过滤制剂中的杂质。The microfluidic encapsulation unit and the TFF liquid change unit, as well as the TFF liquid change unit and the preparation unit, are connected/disconnected using a sterile takeover machine/sterile tube sealing machine. Figure 3 shows the TFF fluid exchange unit. The liquid inlet conduit (32) can be connected/disconnected from the microfluidic encapsulation unit (2) through a sterile tube taking machine/sterile tube sealing machine. The reflux fluid conduit (33) can be connected/disconnected from the preparation unit (3) through a sterile tube taking machine/sterile tube sealing machine. The mRNA liposomes prepared by the microfluidic encapsulation unit flow into the tangential flow filter (31) through the liquid inlet conduit (32). The permeate flows into and out of the tangential flow filter (31) through the permeate conduit (34) to filter impurities in the preparation.
微流控包封单元(2)和TFF换液单元(3)之间还可以通过如图4所示的样品储液 袋(61)转移液体。样品储液袋进液导管(62)、样品储液袋出液导管(64)均可为热塑管,可以用于无菌焊接以传输液体。其中,样品储液袋进液导管(62)与微流控包封单元(2)的出液口可以通过无菌接管机/无菌封管机进行连接/断开,样品储液袋出液导管(64)与进液导管(32)可以通过无菌接管机/无菌封管机进行连接/断开。The sample storage liquid shown in Figure 4 can also be passed between the microfluidic encapsulation unit (2) and the TFF liquid replacement unit (3). The bag (61) transfers liquid. Both the sample liquid storage bag liquid inlet conduit (62) and the sample liquid storage bag liquid outlet conduit (64) can be thermoplastic tubes, which can be used for aseptic welding to transfer liquid. Among them, the liquid inlet conduit (62) of the sample liquid storage bag and the liquid outlet of the microfluidic encapsulation unit (2) can be connected/disconnected through a sterile take-over machine/sterile sealing machine, and the liquid outlet of the sample liquid storage bag The conduit (64) and the liquid inlet conduit (32) can be connected/disconnected through a sterile tube taking machine/sterile tube sealing machine.
TFF换液单元(3)和制剂单元(4)之间采用无菌接管机/无菌封管机进行连接/断开。TFF换液单元(3)和制剂单元(4)之间之间还可以通过如图5所示的制剂储液袋(71)转移液体。其中,制剂储液袋进液导管(72)与可以与TFF换液单元(3)通过无菌接管机/无菌封管机进行连接/断开。制剂储液袋(71)中的制剂经灌装泵管(74)流向灌装针(75),其中灌装泵管(74)可以安装蠕动泵以泵输液体。β袋(76)套在灌装泵管(74)和灌装针(75)的外面,袋体与灌装泵管(74)接触的地方采用焊接方式连接,以确保β袋是全封闭状态;β袋上附接有快速传递接口(RTP)的β阀(77)从而和制剂单元(4)无菌连接。The TFF liquid changing unit (3) and the preparation unit (4) are connected/disconnected using a sterile tube taking machine/sterile tube sealing machine. Liquid can also be transferred between the TFF liquid changing unit (3) and the preparation unit (4) through the preparation liquid storage bag (71) as shown in Figure 5. Among them, the liquid inlet conduit (72) of the preparation liquid storage bag can be connected/disconnected from the TFF liquid exchange unit (3) through a sterile tube taking machine/sterile tube sealing machine. The preparation in the preparation storage bag (71) flows to the filling needle (75) through the filling pump tube (74), where a peristaltic pump can be installed on the filling pump tube (74) to pump liquid. The β bag (76) is placed outside the filling pump tube (74) and the filling needle (75). The contact areas between the bag body and the filling pump tube (74) are connected by welding to ensure that the β bag is fully enclosed. ; The beta valve (77) of the rapid transfer interface (RTP) is attached to the beta bag so as to be aseptically connected to the preparation unit (4).
实施例2:用于制备mRNA脂质体的系统的使用方法Example 2: Method of use of system for preparing mRNA liposomes
1、防爆对接1. Explosion-proof docking
将防爆区各部件通过防爆接头对接。Connect all components in the explosion-proof area through explosion-proof joints.
2、流体对接;2. Fluid docking;
将配液单元、包封单元、换液单元以及制剂单元各部件通过流体管路对接。Connect the components of the liquid preparation unit, encapsulation unit, liquid replacement unit and preparation unit through fluid pipelines.
3、样品取样3. Sample sampling
取样头(55)及(65)可以取样对样品进行监测。The sampling heads (55) and (65) can take samples for monitoring.
4、缓冲液保存及转移4. Buffer storage and transfer
将液体泵入储液袋(51)后可以关闭储液袋管夹(53),以储存缓冲液。转移溶液时,可以打开储液袋管夹(53),并通过储液袋出液导管(54)无菌对接以转移缓冲液。After the liquid is pumped into the storage bag (51), the pipe clamp (53) of the storage bag can be closed to store the buffer solution. When transferring the solution, the pipe clamp (53) of the liquid storage bag can be opened and the buffer can be transferred through the sterile docking of the liquid storage bag outlet conduit (54).
5、样本液保存及转移5. Storage and transfer of sample solutions
将样品泵入样品储液袋(61)后可以关闭样品储液袋管夹(63),以储存样品液。转移溶液时,可以打开样品储液袋管夹(63),并通过样品储液袋出液导管(64)无菌对接以转移样品液。 After pumping the sample into the sample liquid storage bag (61), the sample liquid storage bag pipe clamp (63) can be closed to store the sample liquid. When transferring the solution, the pipe clamp (63) of the sample storage bag can be opened and connected aseptically through the outlet conduit (64) of the sample storage bag to transfer the sample liquid.
实施例3:用于制备mRNA脂质体的步骤Example 3: Steps for preparing mRNA liposomes
步骤1.在防爆配液单元(1)对mRNA原液进行复融,配制含mRNA溶液的水相和用于包封mRNA的有机相。Step 1. Remelt the original mRNA solution in the explosion-proof liquid preparation unit (1), and prepare the aqueous phase containing the mRNA solution and the organic phase used to encapsulate the mRNA.
步骤2.防爆配液单元配制的溶液经过滤器(57)过滤后流入储液袋(51)。Step 2. The solution prepared by the explosion-proof liquid preparation unit is filtered by the filter (57) and then flows into the liquid storage bag (51).
步骤2.1.可选择地,打开取样头(55)对储液袋(51)中的溶液取样检测。Step 2.1. Optionally, open the sampling head (55) to sample and detect the solution in the liquid storage bag (51).
步骤3.将储液袋(51)中的溶液泵入包封单元(2),如微流控包封单元。包封单元对mRNA进行包封,形成脂质体。Step 3. Pump the solution in the liquid storage bag (51) into the encapsulation unit (2), such as a microfluidic encapsulation unit. The encapsulation unit encapsulates the mRNA to form liposomes.
步骤4.将包封后的脂质体溶液引入换液单元(3)。可以将进液导管(32)直接与微流控包封单元直接连接,可选择地,也可以通过样品储液袋(61)转移液体。切向流过滤器(31)对脂质体进行换液操作。Step 4. Introduce the encapsulated liposome solution into the liquid replacement unit (3). The liquid inlet conduit (32) can be directly connected to the microfluidic encapsulation unit. Alternatively, the liquid can also be transferred through the sample storage bag (61). The tangential flow filter (31) performs a liquid exchange operation on the liposomes.
步骤4.1.可选择地,打开取样头(65)对样品储液袋(61)中的溶液取样检测。Step 4.1. Optionally, open the sampling head (65) to sample and detect the solution in the sample storage bag (61).
步骤5.将换液后的脂质体溶液引入制剂储液袋(71)。脂质体经灌装泵管(74)和灌装针(75)灌装进分装瓶中。Step 5. Introduce the changed liposome solution into the preparation storage bag (71). The liposomes are filled into the dispensing bottle through the filling pump tube (74) and the filling needle (75).
以上所述的具体实施例,对本申请的目的、技术方案和有益效果进行了进一步详细说明,应理解的是,以上所述仅为本申请的具体实施例而已,并不用于限制本申请,凡在本申请的精神和原则之内,所做的任何修改、等同替换、改进等,均应包含在本申请的保护范围之内。 The above-mentioned specific embodiments further describe the purpose, technical solutions and beneficial effects of the present application in detail. It should be understood that the above-mentioned are only specific embodiments of the present application and are not intended to limit the present application. Within the spirit and principles of this application, any modifications, equivalent replacements, improvements, etc. shall be included in the protection scope of this application.

Claims (17)

  1. 一种制备mRNA脂质体的系统,其特征在于,其按照连接顺序依次包含配液单元、包封单元、换液单元以及制剂单元;其中所述系统为全封闭系统。A system for preparing mRNA liposomes, characterized in that it includes a liquid preparation unit, an encapsulation unit, a liquid exchange unit and a preparation unit in order of connection; wherein the system is a fully closed system.
  2. 如权利要求1所述的系统,其特征在于,所述配液单元为防爆配液单元。The system of claim 1, wherein the liquid dispensing unit is an explosion-proof liquid dispensing unit.
  3. 如权利要求1或2所述的系统,其特征在于,所述包封单元通过薄膜水化法、挤出法、均质法或者微流控混合进行包封。The system according to claim 1 or 2, wherein the encapsulation unit is encapsulated by a film hydration method, an extrusion method, a homogenization method or a microfluidic mixing method.
  4. 如权利要求3所述的系统,其特征在于,所述包封单元为流体混合包封单元。The system of claim 3, wherein the encapsulation unit is a fluid mixing encapsulation unit.
  5. 如权利要求4所述的系统,其特征在于,所述流体混合包封单元为微流控包封单元。The system of claim 4, wherein the fluid mixing encapsulation unit is a microfluidic encapsulation unit.
  6. 如权利要求5所述的系统,其特征在于,所述微流控包封单元的生产厂家选自如下组:Genizer、Precision NanoSystems(PNI)、PreciGenome、Dolomite Microfluidics、迈安纳(上海)仪器科技有限公司以及苏州艾特森制药设备有限公司。The system of claim 5, wherein the manufacturer of the microfluidic encapsulation unit is selected from the following group: Genizer, Precision NanoSystems (PNI), PreciGenome, Dolomite Microfluidics, Maianna (Shanghai) Instrument Technology Co., Ltd. and Suzhou Aitson Pharmaceutical Equipment Co., Ltd.
  7. 如前述权利要求中任一项所述的系统,其特征在于,所述换液单元为切向流过滤换液单元。The system according to any one of the preceding claims, wherein the fluid exchange unit is a tangential flow filtration fluid exchange unit.
  8. 如前述权利要求中任一项所述的系统,其特征在于,不同的单元之间的连接通过无菌接头实现,断开采用无菌阻断器实现。System according to any one of the preceding claims, characterized in that the connection between different units is achieved by sterile connectors and the disconnection is achieved by sterile interrupters.
  9. 如权利要求8所述的系统,其特征在于,所述无菌接头为无菌连接器或无菌接管机;所述阻断器为无菌断开器或无菌封管机。The system according to claim 8, wherein the aseptic joint is a sterile connector or a sterile tube take-over machine; the blocker is a sterile disconnector or a sterile tube sealing machine.
  10. 如权利要求9所述的系统,其特征在于,所述配液单元和所述流体混合包封单元之间的连接通过无菌连接器实现,断开通过无菌断开器实现。The system according to claim 9, wherein the connection between the liquid preparation unit and the fluid mixing and encapsulation unit is realized through a sterile connector, and the disconnection is realized through a sterile disconnector.
  11. 如权利要求9或10所述的系统,其特征在于,所述流体混合包封单元和所述换液单元之间,以及所述换液单元和所述制剂单元之间的连接通过无菌接管机实现,断开通过无菌封管机实现。The system according to claim 9 or 10, characterized in that the connections between the fluid mixing and encapsulation unit and the liquid exchange unit, and between the liquid exchange unit and the preparation unit are through sterile pipes. The disconnection is achieved by a sterile tube sealing machine.
  12. 如权利要求1所述的系统,其特征在于,所述配液单元不是在无菌环境下的。The system of claim 1, wherein the liquid preparation unit is not in a sterile environment.
  13. 如权利要求1所述的系统,其特征在于,所述配液单元之后设置有除菌滤器。The system according to claim 1, wherein a sterilizing filter is provided behind the liquid preparation unit.
  14. 如权利要求1所述的系统,其特征在于,所述包封单元不是在无菌环境下的。 The system of claim 1, wherein the encapsulation unit is not in a sterile environment.
  15. 如权利要求1所述的系统,其特征在于,所述包封单元不包含除菌滤器。The system of claim 1, wherein the encapsulation unit does not contain a sterilizing filter.
  16. 如权利要求1所述的系统,其特征在于,所述包封单元之后不设置除菌滤器。The system of claim 1, wherein a sterilizing filter is not provided after the encapsulation unit.
  17. 如前述权利要求中任一项所述的系统在制备mRNA脂质体中的应用。 Use of a system according to any one of the preceding claims for the preparation of mRNA liposomes.
PCT/CN2023/108173 2022-07-19 2023-07-19 System for preparing mrna liposomes and use thereof WO2024017300A1 (en)

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