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Review

Enabling mRNA Therapeutics: Current Landscape and Challenges in Manufacturing

by
Maryam Youssef
†,
Cynthia Hitti
†,
Julia Puppin Chaves Fulber
and
Amine A. Kamen
*
Department of Bioengineering, McGill University, Montreal, QC H3A 0G4, Canada
*
Author to whom correspondence should be addressed.
†
These authors contributed equally to this work.
Biomolecules 2023, 13(10), 1497; https://doi.org/10.3390/biom13101497
Submission received: 20 September 2023 / Revised: 5 October 2023 / Accepted: 6 October 2023 / Published: 9 October 2023
(This article belongs to the Special Issue RNA Therapeutics)
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Abstract

:
Recent advances and discoveries in the structure and role of mRNA as well as novel lipid-based delivery modalities have enabled the advancement of mRNA therapeutics into the clinical trial space. The manufacturing of these products is relatively simple and eliminates many of the challenges associated with cell culture production of viral delivery systems for gene and cell therapy applications, allowing rapid production of mRNA for personalized treatments, cancer therapies, protein replacement and gene editing. The success of mRNA vaccines during the COVID-19 pandemic highlighted the immense potential of this technology as a vaccination platform, but there are still particular challenges to establish mRNA as a widespread therapeutic tool. Immunostimulatory byproducts can pose a barrier for chronic treatments and different production scales may need to be considered for these applications. Moreover, long-term storage of mRNA products is notoriously difficult. This review provides a detailed overview of the manufacturing steps for mRNA therapeutics, including sequence design, DNA template preparation, mRNA production and formulation, while identifying the challenges remaining in the dose requirements, long-term storage and immunotolerance of the product.

1. Introduction

From the first demonstration of messenger RNA (mRNA) delivery into in vivo models [1] to the development of lipid nanoparticles using ionizable lipids as a delivery system for the first approved siRNA therapeutic [2], decades of fundamental research converged to enable the creation of feasible RNA vaccines and therapeutics. Given the global success demonstrated during the COVID-19 pandemic, the mRNA technology platform is currently in the spotlight and shows considerable potential not only for vaccines, but also for treatment of diseases [3,4,5,6,7]. This promising technology was shown to have incredibly fast development, manufacturing, and roll-out times [8], with the potential of revolutionizing the therapeutic field as a drug with a wide range of applications [9].
mRNA technology relies on the transfer of an mRNA either encoding an antigen or a therapeutic protein of interest into the cytoplasm [3]. This genetic message, once translated, functions to stimulate an immune response or alter a disease state. In contrast to DNA therapeutics, mRNA does not require nuclear entry as expression occurs directly in the cytoplasm. In addition, this eliminates the risk of insertional oncogenesis associated with viral vector and plasmid DNA techniques. Their ability to be manufactured through cell-free systems eliminates the time constraints and possible contaminants associated with traditional viral vector-based gene and cell therapies [10,11]. Therapeutic use of adeno-associated viruses, for example, require high doses that are difficult to accommodate with the current productivity and scalability issues [12], while enzymatic mRNA production is linearly scalable [13], thus achieving the required production more easily. Moreover, a new mRNA product implies a new sequence, but the physicochemical characteristics of an mRNA remain the same, meaning that the manufacturing process can be replicated with minimal changes for a powerful plug-and-play platform [14]. The technology’s versatility allows it a broad potential of therapeutic applications including but not limited to cell reprogramming, gene editing, protein replacement therapy and cancer immunotherapy [3].
Historically, the progression of RNA-based gene and cell therapies has been limited by challenges related to the instability of RNA, the immunogenic response to RNA molecules as well as the delivery of the RNA across the cell membrane. However, several improvements have been made to increase the stability and to reduce the degradation of RNA molecules including base modifications and the emergence of the lipid nanoparticle (LNP) as an advanced tool for the delivery of RNA-based therapeutics [15]. A range of these drugs have reached the pre-clinical and clinical spaces, with the American Society for Gene and Cell Therapy reporting 897 RNA therapeutics in the clinical pipeline as of April 2023 [16]. In addition, the number of publications which mention mRNA therapeutics has been steadily increasing over the past decade, indicating the growth of the field, as shown in Figure 1.
Despite the technology’s potential, mRNA therapeutics have not taken the market by storm as quickly as the vaccines due mainly to different regulatory processes during global health emergencies. Moving forward, mRNA therapeutics will face challenges regarding different manufacturing and regulatory considerations compared to vaccines. The diversity of applications, classifications, and manufacturing protocols when it comes to mRNA therapeutics make streamlining of regulatory approval more difficult [17]. Moreover, immunostimulatory by-products such as double-stranded RNA must be strictly controlled during manufacturing to ensure immunotolerance of the drug for long-term mRNA treatments [18]. Currently, these therapeutics lack a standardized production pipeline across the published literature and within patents, and manufacturing scalability is limited by high costs associated with current good manufacturing practice (cGMP)-grade reagents required for in vitro transcription (IVT) [19]. Long-term treatments with repeated dosing requires affordable drugs of consistent yield and quality.
As such, this review addresses the challenges to enable widespread use of mRNA therapeutics from a manufacturing perspective, focusing on particularities of therapeutics in contrast to what has been established with production and approval of mRNA vaccines. First, we explore the current landscape of applications in the clinical trial space. Next, we discuss the entire manufacturing pipeline, including sequence design and optimization; production and purification of template DNA; production and purification of mRNA; microfluidic techniques for encapsulation in LNPs; and formulation for product stability. Finally, we identify future perspectives in manufacturing and process automation, as well as novel strategies for delivery and targeting.

2. Current Therapeutic Applications of mRNA

In the context of gene and cell therapy, mRNA may be applied to replace or supplement disease genes and proteins. Specifically, mRNA as a tool for the restoration of a gene or protein in monogenic disorders is of interest within the field [20]. For example, a study conducted by Ramaswamy et al. demonstrated the delivery of factor IX encoding mRNA for the treatment of hemophilia B in a mouse model [21]. Similarly, An et al. demonstrated mRNA therapy in mice for the treatment of methylmalonic acidemia in mice using mRNA encoding human methylmalonyl-CoA mutase [22]. There are also several studies which discuss the use of mRNA therapy for cardiac related diseases [23]. For example, Zangi et al. explored the use of mRNA encoding the vascular endothelial growth factor A gene for cardiac tissue repair [24].
Furthermore, there is therapeutic value in the use of mRNA in cancer treatments. In these cases, the mRNA can be used to deliver suicide genes or tumor-associated antigens (TAAs). A 2019 study examined the use of mRNA encoding a suicide gene for colon cancer therapy and was found to be successful at shrinking tumor size in mice models [25]. Several mRNA treatments for rare genetic diseases have also made it into the clinical pipeline in recent years, with companies such as Moderna and Translate Bio occupying the space [26].
Future prospects in the development of personalized gene therapies are promising due to the rapid manufacturing of these molecules. Personalized medicine strategies consider each patients’ genotypic characteristics, which will allow the production of therapies specifically for cancer patients, rare metabolic disease patients and a range of other pathologies [27,28]. From a manufacturing perspective, these personalized medicines may require smaller infrastructure than that established throughout the COVID-19 pandemic due to the scale of production for individual patients rather than global populations. Hospital-based RNA therapeutic programs, to expedite the process of genetic testing to the production of small cGMP grade material, may accommodate the implementation of these personalized therapeutics [29].
Cell therapies, traditionally performed using viral vectors, have also been an active area of development using RNA therapeutics. Specifically, chimeric antigen receptor (CAR) T-cell therapy has been of interest [30]. This process involves the delivery of the CAR to autologous cells using mRNA and re-infusing these cells to the patient after their modification. Several clinical trials have been performed using this method, including ECI-006, MCY-M11 and Descartes-08, which target melanoma, mesothelin-expressing solid tumors and multiple myeloma, respectively [31].
Similarly, the use of in vitro transcribed mRNA for gene editing techniques is growing both in the literature reports and in the clinical applications. This technique involves mRNA which encodes genome editing nucleases, including zinc finger nucleases, CRISPR-associated nucleases and transcription activator-like effector nucleases, and a guide RNA to repair DNA mutations [32]. The mRNA expresses the encoded nuclease in the cytoplasm, which then enters the nucleus alongside the guide RNA. As such, this technique avoids the challenge associated with DNA-mediated approaches of delivering the encoded nuclease genes to the nucleus before expression and translation in the cytoplasm [32]. Several clinical trials have applied this technique, including a trial sponsored by the University of Pennsylvania for the treatment of HIV-1 infected patients [33]. This technology has been successful in primates, as demonstrated by Munusuru et al. in a recent study [34], and is currently being evaluated in clinical trials conducted by Intellia therapeutics [35,36].

Ongoing Clinical Trials

Currently, there are 84 ongoing (not yet recruiting, recruiting, and active) trials evaluating mRNA therapeutics, with the majority targeting cancer (Figure 2). The majority of ongoing clinical trials involve mRNA therapeutics employing the use of lipid nanoparticles or liposomes. Among these lipid-based mRNA therapeutics, a wide variety of treatments are currently being explored, including protein replacement therapy [37,38,39], cancer immunotherapy, personalized cancer vaccines [40,41,42,43], mRNA-encoded monoclonal antibodies [44,45], and gene editing [35,36] (Table 1). This demonstrates the lipid nanoparticle (LNP) technology’s versatility.
Despite the large range of applications, the majority of the lipid-based mRNA therapeutics in ongoing clinical trials are administered intravenously. For immunotherapeutic applications, intravenous administration allows for high antigen production levels as opposed to other administration methods [46]. The advantage of systemic delivery is, however, accompanied by the requirement of manufacturing larger dosages as opposed to tissue-specific delivery. Intravenous administration requires larger volumes of the drug, and typically leads to the accumulation of the drug in the liver [47], which may limit their internalization in the target tissue. For example, where many therapeutics delivered by IV have been evaluated at mRNA doses in the milligram range [48,49,50,51], an intratumorally delivered drug, MEDI1191, was evaluated at mRNA dosages of 0.1–12 μg [52]. Another targeted administration method, inhalation, has also presented potential for both therapeutic and vaccine applications in recent years. Recent advancements in the nebulization and formulation of lipid nanoparticle products for inhalation demonstrate the possibility of an increase in the number of these products [53,54]. Currently, however, ARCT-032 and VX-522, protein replacement therapies for cystic fibrosis, are the only inhalable mRNA therapeutics in ongoing trials [55,56].
Additionally, the need for repeated dosing is clearly illustrated in these current ongoing clinical trials, emphasizing the need for high-yield production processes for mRNA drug products. However, the challenge of chronic dosing of mRNA therapeutics is balanced by its safety profile compared to viral vector therapeutics and its ability to produce high levels of protein intracellularly compared to protein therapeutics [4].
Beyond lipid-based delivery systems, several ongoing clinical trials are currently evaluating the use of dendritic cells pulsed with mRNA for cancer immunotherapy [57,58,59,60,61,62,63,64,65,66,67], mRNA-based T-cell therapies [68,69,70,71,72,73,74], and other carriers including exosomes and VLPs [75,76]. However, this review focuses on the manufacturing of lipid-based mRNA therapeutics due to their ubiquity in the clinical space.

3. Manufacturing Process

mRNA is a negatively charged, single-stranded molecule involved in protein synthesis that typically ranges between 1 and 15 kilobases in length (kb) [77,78]. It consists of a single-stranded open reading frame flanked by untranslated regions (5′-UTR and 3′-UTR), as well as 5′ cap and 3′ polyadenylation (poly(A)) tail sequences [27]. Each of these segments plays an essential role in the function and stability of the mRNA and must be incorporated throughout production. It is also possible to design a cap-independent RNA treatment by using circular RNA and internal ribosome entry sites [79,80,81,82], which implies a separate category of design and manufacturing considerations outside the scope of this review.
The production process of a new mRNA therapeutic can be divided into the following main steps: (1) DNA template sequence design, (2) DNA template production and purification, (3) IVT, (4) mRNA purification, and (5) encapsulation and formulation for delivery and storage, as illustrated in Figure 3.

3.1. Upstream Process: DNA Template Sequence Design

The production process of mRNA therapeutics begins with the design of a DNA template for subsequent IVT. Transcription templates for mRNA synthesis can be in the form of plasmid DNA (pDNA), PCR products or synthetic double-stranded oligonucleotides [83,84]. Typically, the DNA template should include the following elements [85]: promoter sequence, gene of interest (GOI), 5′ and 3′ untranslated regions (UTRs), poly(A) tail. Each element can be modified or selected accordingly to improve the stability and translation of the mRNA, as has been thoroughly explored in other publications [86,87].
Most commonly, the T7 promoter sequence (5′-TAATACGACTCACTATA-3′) is used for recognition by the T7 RNA polymerase during IVT, considered the standard polymerase for manufacturing purposes [88]. If using the cap analog CleanCap AG, an additional A is required at the 3′ end of the promoter sequence for an AGG initiator sequence [89]. If the manufacturer aims to use a different RNA polymerase, such as from T3 or SP6, the corresponding promoter must be present in the DNA template. Additionally, in the case of a plasmid DNA construct, an antibiotic resistance marker sequence for bacterial selection and restriction sites for DNA template linearization are required.
In applications in which the gene of interest encodes for a therapeutic protein, optimization of the coding sequence can be performed to reduce protein immunogenicity and increase protein expression [90]. For instance, codon optimization can lead to more controllable translation and increased mRNA half-life [78,86,90,91]. It has been reported that high GC content increases mRNA stability, ribosome association, and thus translation efficiency [86,92,93]. Optimization of the GC content in the GOI, with concurrent uridine depletion in therapeutic mRNA design, not only improves the elongation rate and translation efficiency, but can also alter RNA secondary structures that can interfere with gene expression [78].
Both the 5′- and 3′-UTRs are indispensable for the stability and translation initiation of the therapeutic mRNA molecule being delivered [94]. The β-globin UTRs have been widely used in both clinical trials and research contexts [95,96]. 5′-UTR features such as the length, sequence elements and secondary structures play an important role in translation initiation during scanning [97], with the average length of 5′-UTR in eukaryotes ranging from ~100 to ~200 nucleotides (nt) in mammals [86]. However, it has been proposed that a shorter 5′-UTR with at least 20 nt minimizes the scanning process and thus maximizes protein expression [86]. Moreover, highly stable secondary structures near the 5′-end should be avoided as they can disrupt ribosome loading and scanning [98,99], and potential upstream start codons should be eliminated to avoid leaky scanning [86]. Selective translation can be achieved by introducing additional sequence elements to the 5′-UTR depending on the therapeutic purpose. In the context of cancer therapy, special 5′-UTR elements capable of translation under nutrient restriction may be needed for intratumor mRNA injection [86].
The 3′-UTR, similarly to the 5′-UTR, contains regulatory elements that affect translation efficiency and mRNA stability. It is generally believed that a shorter 3′-UTR increases the stability of the mRNA due to the loss of microRNA binding sites, thus escaping mRNA degradation [86]. Additionally, the use of two sequential β-globin 3′UTRs resulted in significantly higher maximum protein levels and prolonged persistence of the protein [100]. Lastly, high throughput techniques have been developed for 3′-UTR optimizations, including a novel cell-based selection process to identify 3′-UTRs that increase protein expression encoded by synthetic mRNA [101] and a massive parallel functional assay for optimization [102].
The poly(A) tail plays a key role in mRNA translation and stability, as it protects the mRNA from nuclease degradation [103]. The poly(A) tail can be added to the mRNA either by using a poly(A) polymerase after transcription or by already having a poly(A) sequence in the DNA template [3]. The latter is the standard practice for clinical applications, as it allows for a consistent, predetermined length of the poly(A) tail [104]. The extension of the poly(A) tail up to 120 nt has been demonstrated to improve translation efficiency, showing that the length is an important aspect to consider [105,106]. Additionally, Trepotec et al. demonstrated the benefit of using segmented poly(A) tails, which consists of at least two A-containing elements of 40–60 adenosines separated by a spacer element of different length. This segmented approach avoids recombination of plasmid DNA during bacterial replication without impairing protein expression and mRNA half-life [107].

3.2. Upstream Process: DNA Template Production

For use in IVT, a linearized and purified DNA template is required. Although there are several approaches for the manufacturing of the template DNA, the space is currently dominated by the use of bacterial fermentation to obtain plasmid DNA. Recently, synthetic and enzymatic approaches have also been proposed for the manufacturing of these templates, including PCR.

3.2.1. Bacterial Fermentation Approach

Plasmid DNA generation is generally performed through fermentation of Escherichia coli (E. coli). Several different strains have been reported for pDNA production such as DH5α [108], DH5 [109], DH10B [110], DH1 [111], JM108 [112], and SCS1-L [113]. Among them, DH5α remains the standard strain used in laboratory and industry practices due to the existence of effective widespread protocols that have been previously established [112]. For this methodology, E. coli competent cells are transformed with the designed DNA plasmids. At the industrial scale, bacterial culture expansion follows three main steps: inoculation for the creation of a master cell bank, shake flask fermentation, and large-scale bioreactor fermentation. To improve pDNA production yields using this production platform, several strategies can be adopted such as selecting a high-producing bacterial strain and/or combining varying medium composition and culture strategies such as batch or fed-batch mode [114].
Vector engineering has contributed to higher yields such as the use of pUC-based plasmids and R1-based plasmids [114]. A study conducted by Lopes et al. demonstrated that a fed-batch mode culture leads to higher plasmid volumetric yields compared to a batch-mode culture [114]. Another study by Carnes et al. demonstrated that using standard high-copy pUC origin-containing plasmids and novel control parameters for fed-batch fermentation resulted in increased specific pDNA yield with respect to cell mass (up to 1500 mg/L of culture medium) compared to 100–250 mg/L for typical plasmid fermentation media and processes [115]. An E. coli DH5α culture in the fed-batch mode, with glucose and glycerol as initial carbon sources in the batch phase, showed a 2.2-fold increase compared to similar feeding phases but with no glycerol [114]. In fact, glycerol is considered a complementary carbon source of glucose because of its high specific plasmid DNA productivity and can be used to increase plasmid yield up to 70.6% [116]. The most used growth medium for E. coli is Luria Broth (LB) with yeast extract as the nitrogen source, although other medium compositions have successfully been used, including a modified MBL medium [116].

3.2.2. Synthetic DNA Approach

To avoid the cloning and preparation steps involved in pDNA production through bacterial fermentation, which are both costly and time consuming, several publications and industrial production platforms have adopted alternative template production methods. The fermentation process can take several days or, at times, several weeks, and it involves expensive reagents, including bacteria and antibiotics [117]. The associated risk of biocontamination in the final product has also become a concern for the good manufacturing practice (GMP) of these therapeutics in the clinical industry [83]. As such, synthetic DNA approaches such as PCR, which allow for time-effective manufacturing, have been used to generate the DNA template for mRNA synthesis [3].
Traditional PCR has successfully been used to produce a DNA template for IVT [118]. In 2022, de Mey et al. introduced a novel approach for the production of mRNA based on a synthetic DNA template generated using assembly PCR with synthetic oligonucleotides [83]. It was reported that using this method, the DNA template amplification can go up to several micrograms, allowing for a fast transition from the DNA production step to the mRNA synthesis in only a few hours [83].
Other synthetic DNA production methods have also been described. For example, Touchlight Genetics Ltd. developed a synthetic DNA manufacturing platform using an in vitro dual enzyme process [117]. This proprietary enzymatic platform enables multi-gram DNA production in weeks, allowing for rapid and large-scale production [117]. However, despite the potential of synthetic DNA template production, these approaches have yet to be established for longer DNA strands. It is crucial to consider not only yield but also the error rate, as mutations should be avoided in the sequence. To produce RNA for therapeutic applications, DNA templates are required to be several kilobases long, and thus bacterial fermentation currently remains most appropriate for these productions.

3.3. Upstream Process: DNA Template Purification

For use in the IVT reaction, the DNA template must be purified and linearized to ensure the quality of the subsequently produced mRNA. The purification process is most extensive in the case of bacterial fermentation. Purification of pDNA from bacterial cells typically begins with an alkaline lysis step after cell harvesting [119,120], in which a detergent solution such as sodium dodecyl sulfate (SDS) and sodium hydroxide are used to disrupt the cell membrane [84]. Next, the lysate is neutralized before clarification [84,119,121]. However, due to the viscous nature of the resulting precipitate, separation of cellular components can only be performed by pre-filtration or centrifugation followed by clearing filtration, which can be time-consuming and expensive [122]. Moreover, DNA sensitivity to shear stress requires low shear stress techniques to gently mix the cell lysate and the neutralizing agent, such as a flotation-based method described in a patent by PlasmidFactory [121,122]. Another method that has been explored for pDNA purification is boiling cell lysis [123], which has been successfully scaled up using a streamlined method of plasmid DNA extraction by continual thermal lysis [124].
In many traditional plasmid DNA purification processes, RNAse enzymes are used to degrade the RNA prior to proceeding with chromatography steps for pDNA isolation [125]. However, RNAse A is purified from bovine components and is of concern in large scale manufacturing [125]. Furthermore, for a process ultimately aiming to produce RNA, the addition of RNAse should be avoided. To this end, RNAse-free purification methods have been proposed: Duval et al. implemented calcium chloride precipitation, followed by tangential flow filtration (TFF) for the removal of high molecular weight RNA and low molecular weight RNA species, respectively [125,126]. These two steps also contribute to the reduction in microbial proteins and chromosomal DNA and to concentration of the product. In addition, performing concentration prior to chromatography reduces column loading time, accelerating the overall process [126].
For pDNA isolation, chromatography steps based on three different principles result in high-purity plasmid free of host DNA, RNA, proteins, and endotoxins: size-exclusion chromatography, ion-exchange chromatography, and hydrophobic interaction chromatography [119,127,128,129,130]. The plasmids can be collected in several isoforms: supercoiled circular isoforms, open circular, and linear. A hydrophobic interaction chromatography method has been proposed to select for supercoiled pDNA, as it is the most stable isoform [130,131].
Finally, the DNA template must be linearized to prepare for mRNA transcription. For the use of the SP6 and T7 RNA polymerase during IVT, a 5′overhang is known to be preferable to ensure the stability of the polymerase and to reduce artifacts [132]. To achieve this overhang after linearization, endonucleases such as HindIII, SpeI, SapI, NotI, EcoRI may be used [133]. Removal of this enzyme as well as of the un-linearized DNA is required to isolate the final DNA template and proceed with transcription. In both laboratory- and industry-scale productions, phenol chloroform extraction has been established as the gold standard technique for this step. However, this technique requires the management of highly hazardous materials and is no longer preferred for large-scale clinical operations [14]. As such, Cui et al. demonstrated a method using positively charged resins for strong anion exchange chromatography, which was deemed comparable to phenol chloroform extraction in terms of the quality of the resulting mRNA [14]. Subsequent TFF allows for removal of smaller impurities while filtering the DNA template into an appropriate solvent for the subsequent IVT [133].

3.4. Upstream Process: mRNA Synthesis

3.4.1. Enzymatic Synthesis

mRNA is produced by IVT, a relatively rapid and simple process in which an RNA polymerase consumes NTPs (nucleotide triphosphates) to catalyse the synthesis of the mRNA from the corresponding DNA linear template. The required components include RNA Polymerase, NTPs, Magnesium (MgCl2), and a reaction buffer. Various bacteriophage polymerases have been used in the field, such as T7, T3, or SP6 RNA polymerases [134]. The T7 RNA polymerase (T7 RNAP) is the most used RNAP in both research and industry, owing to its ability to produce full-length RNA transcripts (longer than 20 kb) with high fidelity [134,135].
Despite its high fidelity and tolerance for incorporation of non-natural NTPs [135], T7 RNAP can also generate immunostimulatory by-products such as double-stranded RNA (dsRNA) which may affect protein expression and render the downstream purification process more difficult [136,137]. Double-stranded RNA molecules are innate immune response activators and should therefore be avoided in therapeutic applications in which immunotolerance to the treatment is important [137,138,139]. The generation of dsRNA by-products can be significantly decreased by engineering a mutant T7 RNAP using computational, structural, mechanistic and laboratory screening approaches. For example, a double-mutant T7 RNAP (G47A + 884G) successfully reduced dsRNA content while maintaining RNA yield and purity [136]. Other advances include the development of thermostable RNA polymerases, such as Hi-T7 RNA Polymerase M0658 by BioLabs, which has been engineered to withstand IVT performed at high temperatures, preventing loopback transcription [140]. However, some experts have noted that high temperatures (≥48 °C) are difficult to scale up and may lead to RNA degradation [136]. Lastly, the addition of urea at a concentration of 1 M during IVT was shown to be an effective method to reduce the undesired nucleobase pairing that causes dsRNA formation [141].
Moreover, magnesium ions are required as a cofactor for the T7 polymerase. Kern et al. found that below 5 mM of free Mg2+, both the transcription rate and IVT efficiency are greatly reduced [142]. However, there is a lack of consensus on the ideal conditions for free Mg2+ concentration. While Sartorius claims that 12–20 mM of MgCl2 per reaction increases mRNA yield [143], Young et al. claim an ideal range between 50 and 60 mM of free Mg2+ [144]. Magnesium counter-ions also have an impact on mRNA yield, with both magnesium acetate and magnesium chloride having been successfully used for IVT [118,145]. A study showed that magnesium acetate is preferred over chloride [145], which was corroborated by Samnuan et al. [146].
The use of modified NTPs such as N1-methylpseudouridine (m1ψ) has been found to reduce the immunogenicity of synthetic mRNA and to drive high levels of protein production, which is in part attributed to its ability to blunt TLR3 activation [135]. The incorporation of other modified nucleotides such as pseudouridine (ψ), 5-methylcytidine (m5C), N6-methyladenosine (m6A), 5-methyluridine (m5U), or 2-thiouridine (s2U) have also shown reduced immunostimulatory effect of the delivered RNA and enhanced translation [135,147,148,149]. The reduction in immune stimulation and increase in stability of the mRNA molecule are especially important in the context of mRNA therapeutics and protein replacement therapies where degradation and lack of translation pose a direct obstacle to the function of the product.
The addition of spermidine to the reaction mixture at a concentration of 1 to 3 mM has been shown to enhance transcription while having an inhibitory effect at higher concentrations [118]. A design of experiment (DoE) performed by Samnuan et al. found that spermidine enhances transcription when present at a concentration of 0.2 to 2 mM [146], further supporting its use.
Mature mRNA requires the 5′ cap structure for mRNA stability and gene expression. A Cap 1 (m7GpppN1mp) structure is preferred for optimal mRNA stability and expression, as it is recognized as self by the immune system [150]. Cap 0 (m7GpppNp), on the other hand, can activate an innate immune response, impairing stability and expression levels [151]. There are two main methods for capping: (1) post-translational capping, where the transcribed mRNA is capped in an additional step using enzymes, or (2) co-transcriptional capping, a one-step process where a Cap analog is incorporated in the IVT reaction.
The vaccinia virus capping enzyme (VCE) is commonly used for enzymatic capping and results in a Cap 0 structure [152]. An additional step using 2′-O-methyltransferase (2′-O-MTase) modifies Cap 0 into a Cap 1 structure [153], reaching a capping efficiency of up to 100% [151]. Moderna has successfully employed this capping strategy in their mRNA-1273 vaccine against SARS-CoV-2 [154]. It is important to note, however, that the addition of several enzymatic steps, including added purification and buffer exchange between the steps, can make the process more difficult to streamline and control [151].
The second capping method uses cap analogs co-transcriptionally, thus reducing production steps. Early iterations of cap analogs had the risk of mRNA elongation in the reverse direction, reducing translation efficiency [155,156]. To avoid this, the anti-reverse cap analog (ARCA) emerged; however, it could only be used to generate constructs with a Cap 0 structure and lower capping efficiency (60–80%) [151,157]. Later, CleanCap technology revolutionized the field as this cap analog allowed for a co-transcriptional addition of the naturally occurring Cap 1 structure at 90–99% efficiency [151], which was successfully implemented in the Pfizer-BioNTech BNT162b2 vaccine against SARS-CoV-2 for emergency use [158]. Cap analogs can lead to a simpler and faster process compared to enzymatic capping, but the use of patented technology can come at a high cost, which should be carefully analyzed in comparison to the cost of enzymatic capping [8].
The IVT reaction may be conducted in both batch and fed-batch modes. The fed-batch mode involves the addition of NTPs and Mg feed during the reaction, as these components have the highest impact on the rate of the reaction as well as the yield [159]. This approach was first demonstrated in 1999 by Kern et al. to produce short RNA molecules [160]. Fed-batch IVT has since been employed on larger mRNA molecules to achieve increased yields [161]. The consumption of NTPs may be monitored using HPLC throughout the duration of the reaction, and they can be supplemented accordingly [159]. Both exceedingly low and high NTP concentrations have been shown to be limiting to the production of RNA, thus supporting the approach to control NTP levels throughout production [146]. This method has previously led to mRNA production with yields of up to 12 g/L [159] compared to the usual 5 g/L [19], showing the immense potential in process intensification.

3.4.2. Towards Automated Production of mRNA

Although production of mRNA therapeutics in a continuous mode has yet to be implemented, several publications have explored this perspective [8,162,163,164]. The intensification of mRNA manufacturing by integrating production and purification in a continuous manner could decrease the hold times and freeze–thaw cycles during the process, potentially increasing the quality and yield of the final product. This could address the challenge in obtaining a higher amount of product with low immunogenicity required for the repeated dosing of mRNA therapeutics. Self-amplifying RNA (saRNA) has been proposed as a modality to reduce manufacturing burden and costs, as a lower dose is required to reach the same level of protein expression as conventional mRNA [19]. However, it is important to note that saRNA can have immunogenic effects [165] that would make it undesirable for chronically dosed treatments.
Continuous processes require the implementation of controls throughout the production to validate the product and to facilitate their automation. Well-defined process models are vital in the transition to continuous automated production. To this end, Helgers et al. produced in silico models for the continuous production of mRNA in plug flow and continuously stirred tank reactors and determined a theoretical improvement factor of 56 times for the space-time yield in comparison to batch production in a continuously stirred tank reactor [162]. Vetter et al. also suggested that the use of control loops, such as proportional integral derivative (PID) control, can be key to improving productivity, robustness and compliance with critical quality attributes (CQA) [163]. Rosa et al. and Ouranidis et al. produced digital designs and conceptual designs for the continuous end-to-end manufacturing of mRNA therapeutics, establishing the initial frameworks for future experimental work to build upon these initial approaches [8,164].

3.4.3. Solid-Phase Synthesis

First established in 1963 by Merrifield for the production of peptides [166], the chemical synthesis method was adapted to the production of short oligonucleotides and advanced by Beaucage and Caruthers [167,168]. Once scaled up to the industrial scale, this method allowed for the production of oligonucleotides up to the kilogram scale, and it can be fully automated [169,170]. The method relies on phosphoramidite chemistry and involves the cyclical addition of nucleosides in a sequence-specific manner on a solid support [171,172]. However, this method for RNA production is only suitable for short oligomers, with some claiming its ability to form chains of up to 40 nucleotides and others using this method extending up to approximately 100–150 nucleotides [153,173,174]. This renders this method currently unsuitable for mRNA production, but rather, it is appropriate for the production of siRNA, miRNA and anti-sense oligonucleotide (ASO) molecules as a straightforward chemical synthesis. It is possible to generate longer RNA molecules through the synthesis of two separate strands and joining them together through ligation strategies, namely T4 ligase [175,176], but this has not yet reached the efficiency and productivity that is established with enzymatic synthesis of mRNA.

3.5. Downstream Process: mRNA Purification

Isolation of complete mRNA transcripts from reagents and reaction by-products is critical for both product functionality and regulatory considerations. Process-related impurities include residual reagents (DNA template, enzymes, unincorporated NTPs) and by-products (immunogenic dsRNA and aborted mRNA products). DNA, RNA (around 300 kDa per kb [177]) and T7 polymerase (99 kDa [14]) are the larger components, while NTPs and cap analogs are much smaller (less than 1 kDa). The DNA template is typically larger than the mRNA produced, as the linearized plasmid includes a backbone sequence that is not transcribed. The purification of mRNA is essential to ensure immunotolerance and to achieve biologically active and therapeutically administrable mRNA [18].
The removal of the DNA template is typically accomplished via enzymatic digestion with DNAse I prior to other purification steps [8,178,179], followed by inactivation with EDTA. However, industry experts have previously indicated that the use of DNAse I may lead to the small DNA template fragments hybridizing to the final mRNA product [133]. Alternatively, chromatography capture methods have been implemented in some processes to remove the DNA template without digestion. Oligo-dT purification is of particular interest due to its ability to bind the polyA tail of the complete mRNA transcripts, without binding the DNA template, truncated mRNA transcripts, unused nucleotides, and the enzyme [133,180]. Cui et al. demonstrated that Oligo-dT chromatography purification may lead to mRNA recoveries of over 90% [14]. However, Oligo-dT purification may not be sufficient to separate dsRNA from the product and must be followed by polishing chromatography steps in the cases of high dsRNA content [8]. Several other chromatography techniques have been demonstrated for mRNA purification, but they were typically preceded by a TFF step, while the Oligo-dT method was used directly as a capture step for a more streamlined process [14].
For therapeutic applications, an emphasis has been placed on the elimination of dsRNA from the IVT mixture to improve translation efficacy and limit induction of cytokines. Several strategies have been described in the literature to ease the burden on purification by avoiding dsRNA formation throughout the reaction, including the addition of urea or use of modified T7 RNAP, as discussed in the mRNA synthesis section. The gold standard purification method for the removal of dsRNA is high-performance liquid chromatography (HPLC) using an alkylated non-porous polystyrene-divinylbenzene copolymer matrix [181]. A simple method using cellulose has proven successful to selectively remove dsRNA at the small scale [182]. Other methods, such as hydroxyapatite chromatography, core bead chromatography, and anion exchange chromatography, have been explored to improve the scalability of the platform [14]. For example, GSK has previously detailed an RNA purification method using DNAse, TFF, and CaptoCore resins, a core bead chromatography resin [183]. These purification methods may be product dependent; however, it has previously been demonstrated that mRNA recovery using core bead chromatography varies based on the length of the sequence [14].
In summary, multiple scalable chromatography methods have been explored for mRNA purification, with further efforts being made to streamline the process while maintaining a high quality of the product. For large-scale mRNA manufacturing, methods which require heating the mRNA sample or using organic solvents should preferably be avoided [14]. It is crucial that the chosen process ensures low levels of immunostimulatory by-products for chronically dosed therapeutic approaches [151].

3.6. Downstream Process: mRNA Delivery

The delivery of naked mRNA into in vivo models was first performed in 1990 by Wolff et al., demonstrating the feasibility of the technique [1]. Though the delivery of naked RNA has since been conducted in animal models and in clinical trials, these RNAs are unstable and can be easily degraded by ribonuclease enzymes during administration [184,185,186]. Thompson et al. found that higher concentrations of RNA are required to overcome the degradation and clearance of naked RNA in plasma, with over 90% of the RNA being cleared within 30 min of administration [187]. In addition, the size, negative charge, and hydrophilicity of messenger RNA molecules hinder their diffusion across the cell membrane [188]. Phua et al. evaluated the transfection efficiency of naked mRNA through several modes of administration and observed rapidly decreasing expression of the naked mRNA when delivered intravenously or intranasally [184]. This instability has previously been presented as an advantage for the safety profile of these therapeutics, but it nonetheless presents a challenge in their transfection efficiency and their long-term storage. To prevent degradation and facilitate cellular entry for cell and gene therapy applications, mRNA therapeutic delivery systems have been developed. Lipid-based and polymeric delivery of mRNA allowed this technology a successful entrance to the clinical space, with lipid nanoparticles (LNPs) being the most prevalent.
Lipid-based delivery particles have also received a considerable amount of attention in the clinical space, with liposomes being the first FDA approved lipid-based nanocarriers in 1990 [189]. Further progress was achieved when another class of lipid-based nanocarriers, lipid nanoparticles (LNPs), were efficient in RNA delivery in non-human primates [190,191]. Finally, the success of these carriers was exemplified during the SARS-CoV-2 pandemic, with both the BioNTech and Moderna vaccines utilizing LNP technology for the delivery of mRNA vaccines [5]. Furthermore, the expansion of lipid libraries and lipid-like compounds over the past two decades has allowed for the identification of novel lipid nanocarrier compositions for RNA delivery [192].
Liposomes are composed of a singular lipid bilayer with an aqueous core, whereas the lipid nanoparticle contains several lipid layers and microdomains of lipids and the oligonucleotide [193]. Liposomes for nucleic acid delivery range between 20 and 1000 nanometers (nm) in size and are generally composed of a cationic lipid along with stabilizers such as cholesterol [188]. In 1987, the formation of cationic liposomes for nucleic acid delivery was first demonstrated [194]. Despite their success in vitro, permanently charged liposomes were unsuccessful in the clinical space due to toxicity, and neutral lipids were inefficient at encapsulating nucleic acids [195]. The emergence of the ionizable cationic lipid, which acquires a positive charge according to the surrounding pH, surmounted this issue and led to the creation of ionizable LNPs [196].
LNPs first entered the therapeutic space with the approval of Onpattro, an siRNA drug product, in 2018 [2]. The vectors are primarily composed of an ionizable cationic lipid, and are supplemented by helper lipids, polyethylene glycol (PEG)-lipids and cholesterol [197]. Ionizable cationic lipids acquire a positive charge according to the surrounding pH, and thus promote interaction and complex formation with the mRNA [195]. For immunotherapeutic applications, studies have demonstrated that the ionizable lipid chosen should have a pKa value between 6.6 and 6.9 in order to elicit an appropriate immune response [198]. The helper lipids, which are commonly phospholipids, and cholesterol serve to stabilize the nanoparticle and aid in the endosomal escape of the mRNA [199]. PEG-lipids reduce aggregation of the LNPs and prolong the circulation time of the particles once administered. The molar ratio at which the lipid components are mixed is not uniform across mRNA therapeutic products and may impact the biological activity of the drug product. Roces et al. demonstrated that altering the lipid molar ratios impacts both size and zeta potential of the LNPs [200]. These characteristics of the LNP impact the biodistribution and immunogenicity of the drug product and should therefore be optimized according to the application. Studies evaluating lipid-based systems administered through subcutaneous and intramuscular injection have shown clear effects of the size on their uptake [201,202]. A study originating from Moderna demonstrated that LNP sizes between 60 and 150 nm were found to produce strong immune responses in non-human primates [201]. Thus, immunotherapeutic mRNA LNP products are likely to be produced within this range [201].
As previously established, administration of LNPs through intravenous and intramuscular methods leads to non-specific accumulation of the particles in the liver [203]. Consequently, this accumulation may lead to side effects of the vaccine including hepatic inflammation and hepatic necrosis [204], and could limit access for patients with preexisting inflammatory conditions [205]. The ability to redirect mRNA LNP therapeutics to their target tissue is therefore critical in order to reduce off-target effects [206]. Further work to improve the distribution of LNPs to target-specific tissues is ongoing [207]. Most prominently, selective organ targeting (SORT) nanoparticles, developed by Cheng et al., demonstrated that supplementing currently established LNP compositions with specified percentages of charged molecules can alter tissue tropism [208]. Furthermore, the spleen has been shown to be effectively targeted through the use of mRNA coated lipoplexes by adjusting the charge ratio (lipid to RNA) to 1.3:2 [209]. Coating strategies for mRNA LNPs have also been explored [210], including new avenues being PEG coatings for redirection of other nanoparticles from the liver to the target tissue [211,212]. These technologies may reduce dose requirements for mRNA therapeutics intended for expression in specific tissues due to their ability to direct the LNPs rather than their non-specific biodistribution.

3.6.1. Microfluidic Manufacturing of mRNA-LNPs

The lipid concentration, the mRNA concentration, the lipid to mRNA ratio as well as the encapsulation technique impact the particle size, polydispersity, surface charge and RNA encapsulation efficiency, all of which are critical quality attributes of the product and impact the activity of the product [213]. As such, the encapsulation protocol should be carefully optimized to meet these standards.
mRNA LNPs are most commonly formulated using T-junction mixing and microfluidic mixing, with work ongoing to improve the scalability of these processes for clinical applications. At a laboratory scale, sonication and bulk mixing have been used, but they present limitations in reproducibility and scalability [214]. Benchtop instruments such as Precision Nanosystems Spark and Ignite systems have been adopted for mRNA LNP formation, both in laboratories and in the industry. There are, however, a number of publications which have designed custom microfluidic devices for this formulation step.
Table 2 summarizes microfluidic mixers which have been used for the encapsulation of RNA into lipid-based delivery systems. Optimization of the flow rates and flow rate ratios (FRR) for each of the devices are uniquely tailored to the device and have not been generalized across microfluidic designs. However, overall trends concerning the operating parameter have been observed in several publications. For example, Roces et al. confirmed that an increase in overall flow rate results in a decrease in size as well as increases in the FRR [200]. These results were corroborated by Gkionis et al. using a different microfluidic system [215].

3.6.2. mRNA-LNP Formulation

Thermostability and physical stability of mRNA-LNPs remains a challenge in the translation of mRNA therapeutics to the market. In non-urgent applications, as in the case of therapeutic use rather than the case of pandemic use, the product may require long-term storage prior to its use. Furthermore, to improve treatment accessibility and transport, refrigerated or room temperature storage are preferable. Both lyophilized and liquid formulations have been considered for the improvement of mRNA-LNP storage. It has been demonstrated that the choice of buffer and cryopreservatives impact the stability of the LNPs both in liquid and solid formulations. Henderson et al. found that, for example, the Hepes buffer better maintains the morphology of the LNPs after freeze–thaw compared to Tris and PBS [224]. Furthermore, their study found that LNPs stored in Tris buffer lead to improved expression of the delivered gene compared to those stored in PBS and Hepes [224]. Zhao et al. evaluated cryopreservatives in the long-term storage of lipid-like nanoparticles under aqueous, freezing and lyophilized conditions [225]. Their results suggested that, when stored at 4 °C, the particles lose the majority of their delivery efficiency within 5 months of storage. Additionally, they found that sucrose and trehalose outperformed mannitol maintaining the delivery efficiency when freezing in liquid nitrogen [225]. Similar results were obtained concerning the efficacy of both sucrose and trehalose at preserving LNPs throughout freezing for LNPs encapsulating siRNA [226]. Similarly, Kim et al. found that LNPs stored in 10% w/v sucrose in PBS did not lose potency after 1 month of storage. Despite most of the current publications presenting data in support of freezing of mRNA-LNPs rather than aqueous conditions, Zhang et al. previously presented a thermostable aqueous vaccine which remains stable for 7 days at 4 °C and 25 °C [227].
Furthermore, formulations undoubtedly vary based on the target application and administration method as well. For example, for lung delivery through inhalation, the formulation requires nebulization. This process can easily destabilize the mRNA-LNPs, impacting size, encapsulation efficiency and subsequent mRNA expression. While the lipid composition of the LNPs impacts their stability throughout the aerosolization process [228], formulation excipients can also be used to decrease changes in these critical quality attributes throughout the process. A patent from Moderna, for example, has previously described mRNA-LNP formulation variations appropriate for nebulization which include the addition of P188 and sucrose to a Tris buffer [54]. Their formulations were also able to maintain both size and encapsulation efficiency over the course of 19 freeze–thaw cycles [54].
Several studies involving the lyophilization of mRNA-LNPs have also been completed since the evolution of the lipid nanoparticle [229,230,231]. Lyophilization promises the ability to store mRNA-LNP formulations at room temperature without the effects of hydrolysis, as is the case of aqueous formulations [229]. Lamoot et al. found that the addition of 20% sucrose (w/v) in a Tris-based buffer allowed for successful lyophilization without major impacts on LNP size, zeta potential or in vitro expression of the encoded gene [229]. Additionally, Muramatsu et al. found that lyophilization of mRNA LNPs in the presence of sucrose (10% w/v) and maltose (10% w/v) provided long-term stability (for at least 12 weeks) of the formulation both at room temperature and at 4 °C [229]. These results emphasize the need for the evaluation of cryoprotectants and lypoprotectants throughout the manufacturing process of lipid-based mRNA therapeutics.

4. Conclusions and Future Perspectives

The revolution of mRNA technology in vaccination highlighted the potential of mRNA therapeutic development, with over 80 ongoing clinical trials and immense interest from companies. The diverse scope of applications for this powerful tool continue to expand, ranging from gene editing to cancer immunotherapy and protein replacement therapy. Additionally, the technology continues to be further refined as new techniques are studied for tissue-targeting with the idea of tailored UTRs [86] and tissue-specific miRNA control systems [232] for selective mRNA translation, as well as development of nanoparticles for targeted delivery [208]. Innovations are also underway in administration methods, with the convenience of the inhalation route and the specificity of intratumoral injections incentivizing further studies.
However, challenges remain when it comes to manufacturing and commercializing this novel class of therapeutics. The regulatory framework for a drug modality with such diverse applications remains unclear, and further streamlining of the approval process could speed up commercialization of new mRNA products [17]. Classification of RNA-based therapies as gene therapies in the literature is unclear due to the fact that RNA therapeutics do not necessarily lead to modification of the patients’ genetic material [3]. While some literature does not distinguish between RNA therapy and gene therapy [103,233,234,235], others strictly refer to gene silencing and gene delivery via RNA molecules as RNA therapeutics [236]. It is therefore clear that as the number of applications and trials for mRNA-based therapeutics grows, harmonization of these definitions is required across regulatory agencies to establish the necessary requirements and controls for the manufacturing of these products, allowing for a more streamlined roll-out of new mRNA therapeutic products. Manufacturers have to closely monitor how such regulatory requirements and definitions evolve to ensure more effective development and data generation for their product.
Moreover, therapeutics have different dose requirements when compared to vaccines, and thus pose different manufacturing scale requirements. The scale can be as small as hospital-based production for personalized medicine [29], and as extensive as large-scale production for a supply of milligram doses administered multiple times a month. A greater focus on process intensification, especially automated and tightly controlled continuous manufacturing, can lead to higher yields and improved product quality, as well as reducing the dependence on the bottleneck of costly GMP-grade reagents. It is also important to emphasize formulation suitable for long-term storage of mRNA, with further studies of both solid and liquid formulations, as therapeutic drugs are not distributed and administered with the same urgency as vaccines during a pandemic.
Additionally, immunotolerance is a crucial characteristic for many chronically dosed treatments [4]; thus, it is essential to tightly control the levels of immunostimulatory by-products like dsRNA by avoiding its formation [136,140,141] or removing it with an adequate purification pipeline [14,182]. Further progress in synthetic approaches to producing DNA template and long RNA molecules could alleviate the burden on purification and revolutionize the mRNA manufacturing landscape. Overall, as production methods become more well-established and suitable for all these purposes, standardization of mRNA manufacturing in the industry can facilitate regulatory approval and enable consistent product yield and quality.

Author Contributions

Writing—original draft preparation, M.Y. and C.H.; writing—review and editing, M.Y., C.H., J.P.C.F. and A.A.K.; supervision and funding acquisition, A.A.K. All authors have read and agreed to the published version of the manuscript.

Funding

M.Y. is supported by a master’s scholarship from the Natural Sciences and Engineering Research Council of Canada (NSERC) and from Fonds de recherche—Nature et technologies Québec (FRQNT). C.H. is supported by a master’s scholarship from Fonds de recherche—Nature et technologies Québec (FRQNT). J.P.C.F. is supported by a fellowship from the Faculty of Engineering at McGill University. A.A.K. is partially funded through Natural Sciences and Engineering Research Council (NSERC) RGPIN-2021-02691 and Canada Research Chair Grant Number CRC-240394.

Conflicts of Interest

The authors declare no conflict of interest.

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Figure 1. Yearly number of publications mentioning mRNA therapeutics over the past two decades, as of August 2023.
Figure 1. Yearly number of publications mentioning mRNA therapeutics over the past two decades, as of August 2023.
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Figure 2. Distribution of ongoing clinical trials by application, delivery method and administration method. IV: intravenous, IT: intratumoral, IM: intramuscular, ILES: intralesional, SQ: subcutaneous, INH: inhalation, ID: intradermal, N/A: Not Available.
Figure 2. Distribution of ongoing clinical trials by application, delivery method and administration method. IV: intravenous, IT: intratumoral, IM: intramuscular, ILES: intralesional, SQ: subcutaneous, INH: inhalation, ID: intradermal, N/A: Not Available.
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Figure 3. Manufacturing process for mRNA therapeutics: (1) DNA template sequence design and optimization, (2) DNA template production and purification using either bacterial fermentation or synthetic approaches, (3) mRNA synthesis via IVT, (4) mRNA purification, and (5) encapsulation for delivery and storage.
Figure 3. Manufacturing process for mRNA therapeutics: (1) DNA template sequence design and optimization, (2) DNA template production and purification using either bacterial fermentation or synthetic approaches, (3) mRNA synthesis via IVT, (4) mRNA purification, and (5) encapsulation for delivery and storage.
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Table 1. Lipid Carrier-Based mRNA Therapeutics in Ongoing Clinical Trials as of August 2023.
Table 1. Lipid Carrier-Based mRNA Therapeutics in Ongoing Clinical Trials as of August 2023.
Trial IDStatusIndicationTreatment NameDose RegimenAdministration Method
NCT04573140RecruitingAdult glioblastomaAutologous total tumor mRNA and pp65 full-length (fl) lysosomal-associated membrane protein (LAMP) mRNA-loaded DOTAP liposomeEvery 2 weeks (3 cycles), monthly (15 cycles)IV
NCT05097911RecruitingAdvanced Hepatocellular CarcinomaMTL-CEBPADay 1 and Day 8 of a 21-Day Dosing ScheduleIV
NCT05579275RecruitingAdvanced malignant solid tumorsJCXH-212 InjectionEvery 3 weeks (up to 8 cycles)Unspecified
injection
NCT05949775Not yet
recruiting		Advanced Malignant Solid TumoursNeoantigen mRNA Personalized Cancer vaccineEvery 3 weeks (9 cycles)SQ
NCT05978102Not yet
recruiting		Advanced Solid TumorSTI-7349/IL2v mRNAEvery 3 weeksIV
NCT05533697RecruitingAdvanced Solid TumoursmRNA- 4359N/AIM
NCT02872025RecruitingCarcinoma, Intraductal, NoninfiltratingmRNA 27522–4 DosesILES
NCT05659264RecruitingChronic heart failuremRNA-01842 groups: single dose OR 4 doses every 16 weeksIV
NCT05141721RecruitingColorectal neoplasmsGRT-R902 (samRNA), GRT-C901(viral vector)4 doses over first yearIM
NCT05712538RecruitingCystic FibrosisARCT-032Single doseINH
NCT05668741RecruitingCystic FibrosisVX-522Single doseINH
NCT05938387RecruitingGlioblastomaCV09050101 mRNA vaccine7 doses at different intervalsIM
NCT05095727RecruitingGlycogen storage diseasemRNA-3745Single dose. Additional dosages after >21 daysIV
NCT05497453RecruitingHepatocellular CarcinomaOTX-2002At least 2 dosesIV
NCT04710641RecruitingHepatocellular CarcinomaMTL-CEBPA (saRNA)Every 3 weeksIV
NCT05120830RecruitingHereditary AngioedemaNTLA-2002Single doseIV
NCT05933577RecruitingHigh-Risk MelanomaV940Every 3 weeks (up to 9 doses)IM
NCT05295433RecruitingIsolated methylmalonic acidemia (MMA)mRNA-3705Every 2–4 weeksIV
NCT04899310RecruitingIsolated methylmalonic acidemia (MMA)mRNA-3705Every 2–4 weeksIV
NCT03289962Active, not recruitingLocally or Advanced Metastatic CancerRO7198457Every 2 weeksIV
NCT05969041RecruitingMalignant Epithelial TumoursMT-302 (A)Weekly–biweekly doses for first 3 doses. Every 4 weeks subsequentlyIV
NCT05539157Active, not recruitingMalignant solid tumours, etc.JCXH-211Every 4 weeks (up to 3 doses)IT
NCT05714748RecruitingMalignant TumoursEBV mRNA vaccineWeekly (4 doses), followed by a 1-month interval (1 dose)IM
NCT03897881ActiveMelanomamRNA-4157Every 3 weeks (up to 9 doses)IM
NCT05264974Not yet recruitingMelanomaAutologous total tumor mRNA loaded DOTAP liposome vaccineEvery 2 weeksIV
NCT04526899RecruitingMelanomaBNT111N/AIV
NCT03871348Active, not recruitingMetastatic NeoplasmSAR441000N/AIT
NCT05142189RecruitingNon-Small Cell Lung CancerBNT116N/AIV
NCT04442347Active, not recruitingOrnithine Transcarbamylase DeficiencyARCT-810Single doseIV
NCT05526066RecruitingOrnithine Transcarbamylase DeficiencyARCT-810Every 2 weeks (up to 6 doses)IV
NCT04161755Active, not recruitingPancreatic cancerRO7198457Every week (8 Cycles)IV
NCT03953235Active, not recruitingPersonalized cancer vaccine for many cancer typesGRT-R904 (samRNA), GRT-C903 (adenoviral vector)N/AN/A
NCT05130437RecruitingPropionic AcidemiamRNA-3927Every 3 weeksIV
NCT04159103RecruitingPropionic AcidemiamRNA-3927Every 3 weeks (up to 10 doses)IV
NCT04382898RecruitingProstate CancerBNT112N/AIV
NCT05660408Not yet recruitingPulmonary osteosarcomaRNA-LP vaccineEvery 2 weeks (2 cycles), monthly (12 cycles)N/A
NCT03739931RecruitingRelapsed solid tumor malignancies/lymphomamRNA-2752Every 2 weeksIT
NCT04503278RecruitingSolid TumorBNT211- CLDN6 CAR-T/CLDN6 CAR-T(A), CLDN6 RNA-LPXN/AIV
NCT05262530RecruitingSolid TumorBNT142N/AIV
NCT04710043RecruitingSolid TumorBNT152/BNT153N/AIV
NCT04455620RecruitingSolid TumorBNT151N/AIV
NCT03313778Active, not recruitingSolid tumoursmRNA-41579 cycles (once every 3 weeks)IM
NCT03946800Active, not recruitingSolid tumoursMEDI1191Every 3 weeksIT
NCT04683939RecruitingSolid tumours, etc.BNT141N/AIV
NCT04601051RecruitingTransthyretin-Related (ATTR) Familial Amyloid PolyneuropathyNTLA-2001Single doseIV
NCT04534205RecruitingUnresectable Head and Neck Squamous Cell CarcinomaBNT113N/AIV
IV: intravenous, IT: intratumoral, IM: intramuscular, ILES: intralesional, SQ: subcutaneous, INH: inhalation, N/A: Not Available.
Table 2. Microfluidic Designs in Literature for Encapsulation of RNA into Lipid-Based Delivery systems. Q total refers to the total flow rate.
Table 2. Microfluidic Designs in Literature for Encapsulation of RNA into Lipid-Based Delivery systems. Q total refers to the total flow rate.
Microfluidic ArchitectureChannel WidthFlow Rate OperationReferences
Ring Micromixer (Precision Nanosystems)150–280 µm channel widthsQ total = 0.4 mL/min–20 mL/min[216]
Staggered Herringbone Mixers150 µm channel widthQ total = 0.024 mL/min–2.4 mL/min[217]
Y junction entry with baffle mixer (iLiNP)200 µm channel widthQ total = 0.05–0.5 mL/min[218]
Staggered herringbone mixer with Y junction entry200 µm channel widthQ total = 1 mL/min–5 mL/min[219]
Staggered Herringbone mixer200 µm channel widthQ total = 0.4 mL/min–1 mL/min[220]
Staggered Herringbone mixer with Y junction entry200 µm channel widthQ total = 0.02 to 4 mL/min[221]
Baffle Mixer with Y junction entry200 µm channel widthQ total = 0.05 mL/min[222]
Hydrodynamic flow focusing150 µm channel widthQ total = 0.20006–0.8001 mL/min[215]
Spiral Mixing300 µm channel widthQ total = 0.00666 mL/min[223]
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Youssef, M.; Hitti, C.; Puppin Chaves Fulber, J.; Kamen, A.A. Enabling mRNA Therapeutics: Current Landscape and Challenges in Manufacturing. Biomolecules 2023, 13, 1497. https://doi.org/10.3390/biom13101497

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Youssef M, Hitti C, Puppin Chaves Fulber J, Kamen AA. Enabling mRNA Therapeutics: Current Landscape and Challenges in Manufacturing. Biomolecules. 2023; 13(10):1497. https://doi.org/10.3390/biom13101497

Chicago/Turabian Style

Youssef, Maryam, Cynthia Hitti, Julia Puppin Chaves Fulber, and Amine A. Kamen. 2023. "Enabling mRNA Therapeutics: Current Landscape and Challenges in Manufacturing" Biomolecules 13, no. 10: 1497. https://doi.org/10.3390/biom13101497

APA Style

Youssef, M., Hitti, C., Puppin Chaves Fulber, J., & Kamen, A. A. (2023). Enabling mRNA Therapeutics: Current Landscape and Challenges in Manufacturing. Biomolecules, 13(10), 1497. https://doi.org/10.3390/biom13101497

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