Recent progress in drying technologies for improving the stability and delivery efficiency of biopharmaceuticals.

✅ 全文

干燥技术在提高生物制品稳定性和递送效率方面的最新进展

作者 Emami Fakhrossadat; Keihan Shokooh Mahsa; Mostafavi Yazdi Seyed Jamaleddin 期刊 Journal Of Pharmaceutical Investigation 发表日期 2023 卷/期/页码 Vol. 53(1) ISSN 2093-5552 DOI 10.1007/s40005-022-00610-x 类型 原创研究 (Original Research)

📄 中文摘要 Chinese Abstract

中文
生物制药(包括蛋白质、多肽、疫苗和单克隆抗体)通常以液体制剂形式存在,其稳定性低于固体剂型。为在储存和运输过程中保持其理化完整性和生物活性,有效的干燥技术至关重要。多种方法——如冷冻干燥(FD)、喷雾干燥(SF)、喷雾冷冻干燥(SFD)、超临界流体干燥(SCFD)及其他技术——被用于将这些不稳定的生物分子转化为稳定的固体粉末。干燥方法的选择取决于生物分子的特性、预期给药途径(如肺部、鼻腔、注射)以及工艺经济性。可吸入干粉制剂为呼吸系统和全身性疾病提供了非侵入性给药方式,可减少治疗剂量和成本,同时避免冷链需求。

📋 英文结构化总结 English Structured Summary

全文整理

EN

Background:

Biopharmaceuticals, including proteins, peptides, vaccines, and monoclonal antibodies, are often formulated in liquid dosage forms that exhibit lower stability than solid forms. To preserve their physicochemical integrity and biological activity during storage and transport, effective drying techniques are essential. Various methods—such as freeze drying (FD), spray drying (SD), spray freeze drying (SFD), supercritical fluid drying (SCFD), and others—are employed to convert these labile molecules into stable solid-state powders. The choice of drying method depends on the biomolecule’s properties, intended route of administration (e.g., pulmonary, nasal, parenteral), and process economics. Inhalable dry powder formulations offer non-invasive delivery for both respiratory and systemic diseases, reducing therapeutic doses and costs while avoiding cold-chain requirements.

Methods:

This review synthesizes recent advances in drying technologies for biopharmaceuticals, drawing from full-text analysis of peer-reviewed literature. It evaluates methodologies including FD, SD, SFD, SCFD, thin-film freeze drying (TFFD), and emerging techniques like PRINT® and fluidized bed drying. The review also examines characterization strategies for dried powders, encompassing physical properties (e.g., particle size, morphology, residual moisture), aerosol performance (via cascade impingers), and protein stability assessments using spectroscopic and calorimetric techniques. Clinical trial data and FDA-approved products are analyzed to contextualize translational progress.

Results:

Freeze drying remains dominant but is limited by long processing times and high energy use; novel excipients like dextran improve thermal stability and reduce aggregation in monoclonal antibodies. Spray drying enables continuous, scalable production with acceptable siRNA integrity despite thermal/shear stress, though biological activity may slightly decrease. Spray freeze drying yields porous, homogenous particles ideal for inhalation, with amino acids (e.g., leucine, phenylalanine) and trehalose effectively stabilizing IgG during processing and storage. Supercritical fluid drying using scCO₂ produces solvent-free, morphologically controlled microparticles, with leucine enhancing aerosol performance. Thin-film freeze drying achieves high aerosolizable mAb powders (FPF >90%) when formulated with lactose/leucine in PBS. Emerging methods like PRINT® allow precise control over particle geometry for targeted delivery.

Data Summary:

In TFFD studies, 1% IgG with lactose/leucine (60:40 w/w) in PBS achieved a fine particle fraction (FPF) of 92.64 ± 1.311%. SFD formulations with trehalose and phenylalanine limited IgG aggregation to <2.2% and maintained stability at 40°C/75% RH for two months. SCFD-optimized particles with 13% leucine reached an FPF of 27.8 ± 0.4%. In SD, siRNA entrapment ranged from 77–93%, with decomposition as low as 20% due to rapid solvent evaporation. Residual moisture in freeze-dried IgG was ≤4% w/w, increasing with storage temperature. Aerodynamic diameters of dried powders were generally within 1–5 µm, suitable for pulmonary deposition.

Conclusions:

Drying technologies significantly enhance the stability, shelf life, and delivery efficiency of biopharmaceuticals. Process parameters and excipient selection must be tailored to the specific protein and administration route. While FD is well-established, SD and SFD offer scalability and superior aerosol characteristics for inhalation. SCFD and TFFD show promise for producing high-performance powders with minimal degradation. Advances in analytical characterization ensure comprehensive evaluation of powder properties, conformational stability, and bioactivity, supporting robust formulation development.

Practical Significance:

These drying technologies enable the development of stable, non-invasive, inhaled biopharmaceuticals for treating respiratory conditions (e.g., Parkinson’s with INBRIJA®) and systemic diseases (e.g., diabetes, hormone deficiencies), reducing reliance on injections and cold-chain logistics. They support global vaccine distribution (e.g., mRNA COVID-19 vaccines) and facilitate targeted cancer therapies (e.g., siRNA/doxorubicin co-delivery systems), offering cost-effective, patient-friendly alternatives with broad pharmaceutical and clinical applicability.

📋 中文结构化总结 Chinese Structured Summary

中文

背景:

生物制药(包括蛋白质、多肽、疫苗和单克隆抗体)通常以液体制剂形式存在,其稳定性低于固体剂型。为在储存和运输过程中保持其理化完整性和生物活性,有效的干燥技术至关重要。多种方法——如冷冻干燥(FD)、喷雾干燥(SF)、喷雾冷冻干燥(SFD)、超临界流体干燥(SCFD)及其他技术——被用于将这些不稳定的生物分子转化为稳定的固体粉末。干燥方法的选择取决于生物分子的特性、预期给药途径(如肺部、鼻腔、注射)以及工艺经济性。可吸入干粉制剂为呼吸系统和全身性疾病提供了非侵入性给药方式,可减少治疗剂量和成本,同时避免冷链需求。

方法:

本综述基于对同行评审文献的全文分析,综合了生物制药干燥技术的最新进展。评估的方法包括FD、SD、SFD、SCFD、薄膜冷冻干燥(TFFD)以及PRINT®和流化床干燥等新兴技术。综述还探讨了干燥粉末的表征策略,涵盖物理性质(如粒径、形态、残留水分)、通过级联撞击器评估的气溶胶性能,以及利用光谱和量热技术进行的蛋白质稳定性分析。同时分析了临床试验数据和FDA批准产品,以阐明转化研究进展。

结果:

冷冻干燥仍占主导地位,但受限于较长处理时间和较高能耗;新型辅料(如葡聚糖)可提高单克隆抗体的热稳定性并减少聚集。喷雾干燥可实现连续化、规模化生产,尽管存在热/剪切应力,siRNA完整性仍可接受,但生物活性可能略有下降。喷雾冷冻干燥可产生适用于吸入给药的多孔均一颗粒,氨基酸(如亮氨酸、苯丙氨酸)和海藻糖在加工和储存过程中能有效稳定IgG。使用scCO₂的超临界流体干燥可制备无溶剂、形态可控的微粒,亮氨酸可增强气溶胶性能。薄膜冷冻干燥在PBS中以乳糖/亮氨酸为辅料时,可获得高可雾化单克隆抗体粉末(FPF >90%)。PRINT®等新兴方法可精确控制颗粒几何结构以实现靶向递送。

数据总结:

在TFFD研究中,含1% IgG、乳糖/亮氨酸(60:40 w/w)的PBS配方实现了92.64 ± 1.311%的细颗粒分数(FPF)。含海藻糖和苯丙氨酸的SFD配方将IgG聚集率控制在<2.2%,并在40°C/75% RH条件下保持稳定性达两个月。含13%亮氨酸的SCFD优化颗粒FPF达27.8 ± 0.4%。在SD中,siRNA包封率为77–93%,因快速溶剂蒸发导致的分解率低至20%。冻干IgG的残留水分≤4% w/w,且随储存温度升高而增加。干燥粉末的空气动力学直径通常在1–5 µm范围内,适合肺部沉积。

结论:

干燥技术显著提高了生物制药的稳定性、保质期和递送效率。工艺参数和辅料选择需根据特定蛋白质和给药途径进行定制。尽管FD技术成熟,SD和SFD在吸入给药方面具有可扩展性和更优的气溶胶特性。SCFD和TFFD在制备高性能、低降解粉末方面展现出良好前景。分析表征技术的进步确保了粉末特性、构象稳定性和生物活性的全面评估,支持稳健的制剂开发。

实际意义:

这些干燥技术推动了稳定、非侵入性吸入式生物制药的开发,用于治疗呼吸系统疾病(如帕金森病的INBRIJA®)和全身性疾病(如糖尿病、激素缺乏症),减少了对注射和冷链物流的依赖。它们支持全球疫苗分发(如mRNA新冠疫苗),并促进靶向癌症治疗(如siRNA/阿霉素共递送系统),提供了具有广泛制药和临床适用性的经济高效、患者友好的替代方案。

📖 英文全文 English Full Text

EN

3814 phenaturepg Journal of Pharmaceutical Investigation J Pharm Investig PMC9768793 9768793 9768793 36568503 10.1007/s40005-022-00610-x Recent progress in drying technologies for improving the stability and delivery efficiency of biopharmaceuticals Emami Fakhrossadat 1 ✉ # Keihan Shokooh Mahsa 1 # Mostafavi Yazdi Seyed Jamaleddin 2 # 1 College of Pharmacy, Tehran University of Medical Sciences, Tehran, Iran 2 Department of Mechanical Engineering, Kettering University, 1700 University Ave, Flint, MI 48504 USA ✉ Corresponding author. # Contributed equally. 21 12 2022 53 1 35 35–57 21 12 2022 © The Author(s) under exclusive licence to The Korean Society of Pharmaceutical Sciences and Technology 2022, Springer Nature or its licensor (e.g. a society or other partner) holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. This article is made available via the PMC Open Access Subset for unrestricted research re-use and secondary analysis in any form or by any means with acknowledgement of the original source. These permissions are granted for the duration of the World Health Organization (WHO) declaration of COVID-19 as a global pandemic. Abstract Background Most biopharmaceuticals are developed in liquid dosage forms that are less stable than solid forms. To ensure the stability of biopharmaceuticals, it is critical to use an effective drying technique in the presence of an appropriate stabilizing excipient. Various drying techniques are available for this purpose, such as freeze drying or lyophilization, spray drying, spray freeze-drying, supercritical fluid drying, particle replication in nonwetting templates, and fluidized bed drying.

Area covered In this review, we discuss drying technologies and their applications in the production of stable solid-state biopharmaceuticals, providing examples of commercially available products or clinical trial formulations. Alongside this, we also review how different analytical methods may be utilized in the evaluation of aerosol performance and powder characteristics of dried protein powders. Finally, we assess the protein integrity in terms of conformational and physicochemical stability and biological activity. Expert opinion With the aim of treating either infectious respiratory diseases or systemic disorders, inhaled biopharmaceuticals reduce both therapeutic dose and cost of therapy. Drying methods in the presence of optimized protein/stabilizer combinations, produce solid dosage forms of proteins with greater stability. A suitable drying method was chosen, and the process parameters were optimized based on the route of protein administration. With the ongoing trend of addressing deficiencies in biopharmaceutical production, developing new methods to replace conventional drying methods, and investigating novel excipients for more efficient stabilizing effects, these products have the potential to dominate the pharmaceutical industry in the future. Keywords: Stability, Biopharmaceuticals, Characterization, Solid-dosage form, Drying status released display-pdf yes is-in-collection-domain yes is-olf no is-manuscript no is-preprint no is-journal-matter no is-scanned no is-retracted no Received 2022 Aug 17; Accepted 2022 Dec 12; Issue date 2023. Introduction In recent decades, biopharmaceuticals, including peptides, proteins, vaccines, genes, hormones, and enzymes (Sharma et al. 2021 ; O’Sullivan et al. 2022a , b ) have experienced rapid growth in their production (Chen et al. 2021a , b ). Biopharmaceutical drugs have accounted for 35% of all FDA-approved products over the past 16 years (Vass et al. 2019 ), and it is projected that by 2025, this market will be worth $395 billion (Guo et al. 2020 ). Accordingly, overcoming the challenges in formulating these biopharmaceuticals is of immense importance. The large size, complex structure, and susceptibility of therapeutic proteins to environmental stress result in several physicochemical degradations, such as deamidation, oxidation, hydrolysis, racemization, isomerization, β-elimination, disulfide exchange, aggregation, precipitation, and denaturation (Filipe et al. 2013 ). Given the low oral bioavailability of these formulations and their limited transport through the epithelium, parenteral administration is an intriguing prospect (Anselmo et al. 2019 ). The most common route of administration is parenteral administration, which frequently uses a liquid dosage form for delivery (Zhang et al. 2021a , b ); however, more stable products can be obtained in solid dosage forms (Fig.  1 ) (Chen et al. 2021a , b ). Thus, to retain the physicochemical integrity and intrinsic activity of the product (Vass et al. 2019 ; Mutukuri et al. 2021 ), methods of solid-state formulation must be developed (Mutukuri et al. 2021 ). Fig. 1 The schematic figure compares biopharmaceuticals delivery via different routes of administration and shows how pulmonary and/or nasal delivery outweighs parenteral (Kunde et al. 2022 ) In liquid form, biomolecule instability can lead to permanent or reversible changes in drug during the storage, transportation, and administration (Vass et al. 2019 ; O’Sullivan et al. 2022a , b ). Various methods have been applied to stabilize biopharmaceuticals, such as glycosylation (O’Sullivan et al. 2022a , b ), lipidation (Egli et al. 2021 ), and the incorporation of new ingredients. However, many applied stabilization technologies are expensive and lead to unwanted effects on the structure and specificity of some biomolecules. To improve stability, drying techniques (O’Sullivan et al. 2022a , b ) such as freeze drying (FD), spray drying (SD), spray freeze drying (SFD), supercritical fluid drying (SCFD), and critical fluid SD, can be applied to eliminate water and provide the product in a more stable state in powder form (Vass et al. 2019 ) with a longer shelf life (Keil et al. 2019 ). Drying methods result in more convenient handling of the final products and minimize the expense of supplying a cold chain (2 to 8 °C) or sometimes freezing (− 20 to − 80 °C) during transportation and storage (O’Sullivan et al. 2022a , b ). In our previous study, we reported different drying technologies and stabilizing excipients available to stabilize biopharmaceuticals (Emami et al. 2018a , b ). In this review, we discuss the recent drying techniques used to produce dry powder formulations of biopharmaceuticals, as well as characterization tests for therapeutic proteins. Alongside this, we also review that dried powder inhalers have mainly focused on local drug delivery for treating respiratory diseases. Aside from patients suffering from pulmonary diseases benefiting from local drug delivery through inhalation, those patients with diabetes, osteoporosis, and hormone deficiency (Keyhan shokouh et al. 2021 ) could enjoy the simplicity and non-invasiveness of such administration way (Emami et al. 2018a , b ; Emami et al. 2019 ; Dhahir et al. 2021 ). Drying techniques Choosing a suitable drying technique from various methods depends on the native features of the given biomolecules, desired route of their administration, and the expenses of the drying procedure (Vass et al. 2019 ) (Fig.  2 ). Fig. 2 Summary of the parameters influencing the characteristics of dried proteins Freeze drying (FD) FD, lyophilization, is the most common applied dehydration technology consisting of three main steps (1) freezing, (2) primary drying, and (3) secondary drying. Included variables in the FD process from the rate of decreasing temperature in the freezing stage and increasing temperature to a certain point in sublimation to the rate at which temperature reduces and the frequency of temperature cycles can affect the final product characteristics such as crystallinity, crystal size, pore size, and even structural stability (O’Sullivan et al. 2022a , b ). Despite its shortfalls such as high energy and time consumption (from days to weeks to complete) (Vass et al. 2019 ), induced stresses in freezing and thawing stages, and lack of control over the size of the resultant particles (O’Sullivan et al. 2022a , b ), FD is widely applied to produce more than half of the present biopharmaceuticals in today's market (Vass et al. 2019 ). Freeze dried products include monoclonal antibodies (mAbs) for either inhalation or injection purpose (Hickey et al. 2022 ), high protein concentration products for targeted delivery systems (Butreddy et al. 2021 ), vaccines [DNA (Chen et al. 2021a , b ), mRNA (Cohen 2022 ), siRNA- and mRNA (Zhao et al. 2020 ) based therapeutics (Rehman et al. 2021 ; Tang et al. 2021 )], and room-temperature stable mAb solutions (Zhang et al. 2021a , b ). Conventional excipient, with low glass transition (Tg) and low collapse temperature (Tc) such as sucrose can lead to a long and expensive lyophilization cycle, which could be substituted with new excipients, e.g., dextran (Haeuser et al. 2020 ). Thin-film freeze drying (TFFD) is a cryogenic technology applying an intermediate freezing rate from 10 2 to 10 3  k/s somewhere between SFD (10 2  k/s) and lyophilization (1 k/s) (Engstrom et al. 2008 ) to engineer aerosolized dry powder from the liquid form to deliver drugs to the lungs (Hufnagel et al. 2022 ). At a relatively high freezing rate, such as in TFFD, dissolved solute particle aggregation and precipitation as any form of dispersion can be avoided. Moreover, this high yield technique can produce homogenous particle size distribution, and a low-density brittle matrix composed of microparticle-sized nanoaggregates is favored for the respiratory delivery system (Sahakijpijarn et al. 2020 ). TFFD has been applied to formulate dry powders of small molecules, proteins, and vaccines (Wang et al. 2021 ). Hufnagel et al. applied TFFD to formulate mAbs, immunoglobulin G (IgG) and anti-programmed cell death protein 1 (anti-PD-1), into dried powders and investigated their aerosol performance. The efficacy of the optimal ratios of two applied excipient groups, trehalose/leucine (75:25 w/w) and lactose/leucine (60:40 w/w), as well as water or phosphate-buffered saline (PBS) as the TFFD solvent were investigated in their studies. In their study, the mAb loadings percentages were 0.5% and 1% IgG, in which 1% IgG with lactose/leucine (60:40 w/w) in PBS showed the best aerosol performance among others; in terms of the solvents, PBS rather than water improved reproducibility and aerosols performance. While trehalose/leucine (75:25 w/w) incorporating 1% IgG formulation displayed a significantly reduced fine particle fraction (FPF) compared to the half of that loaded mAb. Preparing 1% of Anti-PD-1 mAb with the same optimal ratio of lactose/leucine (60:40 w/w) resulted in a dry powder formulation almost as aerosolizable as IgG1-LL-PBS [the recovered FPF for Anti-PD-1 91.38 ± 1.89 and recovered FPF for IgG 92.64 ± 1.311). Furthermore, anti-tumor necrosis factor α (anti-TNF-α) mAb was formulated at 1% w/w (trehalose/leucine 75:25), and interestingly its recovery was reported as a full one, and the monomer content did not change while in the Anti-PD-1 mAb formulation, the FPF experienced a fall to 79.2% from 96% following TFFD process (Hufnagel et al. 2022 ). The time and money-consuming drying step in FD, primary drying, are inevitable with formulations including sucrose as their lyo- and cryoprotectant ingredient. Haeuser et al. investigated how to improve mAbs stability at high temperatures of storage. They utilized different weights of a polysaccharide, dextrans (1, 10, 40, 150, and 500 kDa) alone and in combination with sucrose at different ratios. At higher molecular weight (MW) of dextran (40–500) and dextran to sucrose weight ratios, an increased temperature of 20 °C in Tc compared to sucrose was observed. It caused longer reconstitutions and more viscosities. Moreover, by elevating the dextran weight fraction, a higher degree of cracking of cakes was seen, amplified if a higher weight dextran was used. Adding dextran also resulted in higher Tg values while residual moisture level experienced a decline. Protein stability analysis for mAb1 and mAb2 formulations with pure dextran or dextran/sucrose 1:1 mixture was conducted for two weeks at 40 °C regarding the soluble aggregate formation. According to the results, directly after FD, 100% dextran formulations showed a slight increase of high molecular weight species (HMWs) 1–3%, under 40 °C storage conditions, all formulations showed a remarkable amount of HMWs. In terms of HMWs% in pure dextran formulations, higher MW dextrans showed less HMWs% although they were larger in size compared to HMWs in formulations with lower MW dextrans. mAb1(IgG1, pI ~ 9.4, 148 kDa) and mAb2 (IgG1 pI ~ 8.2, 149 kDa) were formulated with 1:1 dextran/sucrose mixture. Their protein stability analysis displayed no change in HMWs% immediately after FD, although at 40 °C storage, 10–500 kDa dextran containing formulations showed five times lower HMWs% than pure dextran ones. Free terminal glucose of dextrans was the reason for glycation, and a higher percentage of HMWs was noticeably reduced by adding sucrose (Haeuser et al. 2020 ). High concentrated therapeutic proteins have a concentration of 50 to 150 mg/mL. These proteins include plasma-derived immunoglobulins with the typical concentrations of 50–100 mg/mL of IV immunoglobulin. Duraliu et al. assessed the stability of freeze-dried plasma-derived IgG during a 6 to 12 month span under accelerated and real-time storage conditions. (− 20 °C ~  < 5% relative humidity (RH); 20 °C, ~ 40% RH; and 45 °C ~ 10% RH). A range of IgG concentrations from 10 to 200 mg/mL were prepared and in combination with sucrose its concentration was fixed at 10 mg/mL while sucrose/IgG molar ratio varied as follows: 1% IgG, 439:1; 5% IgG, 88:1; 10% IgG, 44:1; 20% IgG 22:1. At the end of the 12 months of storage at − 20 °C, 20 °C, and 45 °C temperatures, all IgG concentrations showed a higher percentage of moisture content, especially at higher temperatures (20 °C and 45 °C). While 10 mg/mL IgG had a moisture content around 3–4% at elevated temperatures, increased concentrations of IgG resulted in less moisture, 1–2% w/w. At 20 °C and 45 °C, the monomer loss was experienced with all IgG concentrations in which the higher concentration have shown the greater monomer loss. Considering binding activity measured by ELISA and by the application of anti-diphtheria and anti-tetanus IgG as markers for IgG, at concentrations of 50 and 100 mg/mL, reduced monomer content with proper binding activity was observed at high temperatures and after 12-month storage. At the same time, the monomer content was decreased under the same condition. The higher IgG concentration (200 mg/mL) had variable ELISA results due to the lack of full reconstitution and over two hours duration for being dissolved (Duralliu et al. 2020 ). Spray drying (SD) Despite several advantages of the FD process to produce dry powders, FD has some limitations. The restriction of FD includes consuming a tremendous amount of time, and energy and resources. In addition, FD has a difficulty in processing massive material quantities, which is critical in pharmaceutical industries. Moreover, handling the characteristics of particles and cake in FD is difficult. These challenges are drivers to look for an alternative drying technique, SD (Pinto et al. 2021 ). Dried powder production via SD technique involves atomizing protein solution into a drying chamber to be dried at once and to form solid particles, all happening in one step. Regarding functional excipients, both techniques share the same stabilizers (Massant et al. 2020 ). However, "continues processing" assigned to the SD makes it an outstanding technique in the pharmaceutical industry to manufacture a large volume of stable, dried powders (Pinto et al. 2021 ). During SD, the temperature and the atomizing gas flow rate are the essentials parameters responsible for particles properties, such as their size, morphology, and residual moisture content (Wu et al. 2019 ). Numerous spray-dried products are either approved or commercially available. Since 2006 when inhaled spray-dried insulin, Exubera®(Pfizer), became commercially available, many investigations have been conducted to produce spray-dried biopharmaceuticals (endocrine hormones, bacteriophage viruses, therapeutic enzymes, etc.) to treat diseases (Pinto et al. 2021 ). Considering excipients and their ratio on storage stability of dried powder and reconstitution time, Massnat et al. used two IgG4 mAbs (mAb1 and mAb2) as the model protein, sugars (trehalose, sucrose), and a range of amino acids including glycine (Gly), alanine (Ala), proline (Pro), serine (Ser), valine (Val), leucine (Leu), isoleucine (Ile), glutamine (Gln), histidine (His), lysine (Lys), arginine (Arg), phenylalanine (Phe), tryptophan (Trp) as their formulation stabilizers. According to the initial results, small neutral and basic as in a sugary basis (sucrose, trehalose) showed reduced reconstitution time and improved stability. In the second part of their study, a design of experiment (DOE) based trial, incorporating 16 formulations, in which an optimum ratio of trehalose/amino acid by employing two groups of essential amino acids (Lys and Arg) and neutral amino acids (Gly and Pro) was put into test. In such a trial, trehalose concentration started from 30 up to 120 mM, and for amino acids, it ranged between 50 and 150 mM. Storage condition was set at 25 °C and 40 °C for 13 consecutive weeks. All formulations preserved their amorphous state except for those containing high Lys or Gly content and low trehalose content. Arg remarkably reduced reconstitution time among tested amino acids and increased storage stability. Whereas, in other formulations with amino acids, the trehalose concentration and the sugar component, played crucial roles in improving stability and reconstitution time. Indeed, the stabilizing effect of Arg was so strong that there was no need to add a sugar stabilizer to enhance the stability. In addition, the weight ratio of mAb to stabilizer should be at least 1:1 (w/w) to obtain the satisfactory stability and reconstitution time. In their study, HMWs, relative humidity (RH), and turbidity results were utilized to evaluate the efficacy of stabilizers on aggregations and storage stability (Massant et al. 2020 ). Wu et al. assessed the efficacy of two significant stresses, thermal and shear, on the chemical integrity, biological activity, yield, and size of particles during SD of enhanced green fluorescent protein-specific short interfering RNA (EGFP-siRNAs) solutions. Accordingly, in terms of siRNA content, all spray-dried powders showed a range of entrapment from 77 to 93%, indicating some extent of siRNA loss during the process, though with an increase in inlet temperature, the entrapment was decreased. A correlation between measured yield and atomization gas flow rate was observed by measuring production yield. However, the effect of inlet air temperature on yield production is variable and dependent on the flow rate. Unfortunately, the chemical integrity of spray-dried siRNAs could be hugely affected by the thermal and shear stress that particles were exposed during the SD process. Based on the results obtained from exposing siRNA solutions to the degrees of temperature close to the outlet temperature, 92 °C, the percentage of decomposed siRNA experienced a 52.9% enhancement and reached 66% when the heating time was changed from 10 to 120 min. Even though the outlet temperatures in the current SD process were as high as 92 °C and 125 °C, short-time exposure of siRNAs and quick evaporation of the solvent resulted in decomposition as low as 20%. According to the transfection efficiency tests, all spray-dried siRNA experienced a lower biological activity than non-spray-dried formulations. Moreover, further experiments did not reveal any correlation between transfection efficiency and chemical integrity. In other words, a small extent of chemical integrity does not compromise the biological activity of spray-dried siRNAs (Wu et al. 2019 ). Spray freeze drying (SFD) SFD is an attractive drying technique comprising of atomizing feeding solution into a cryogenic liquid, e.g., O 2 , N 2, or Ar container, and drying the frozen droplets. Formed particles because of some unique characteristics including homogenous size distribution, porous structure, and improved shelf stability are desirable for pulmonary drug delivery. This method of drying has proved its functionality in enhancing biopharmaceutics classification system (BSC) class II drugs' solubility (Adali et al. 2020 ), producing inhalable dry powders of drugs other than those of the previous group (Liao et al. 2020 ; Faghihi et al. 2021 ), remarkably enhancing dissolution (Hu et al. 2019 ). Although SFD is highly favorable for drying thermo-sensitive materials (Adali et al. 2020 ), induced stresses such as dehydration, cold denaturation, and ice crystallization on mAbs and other biopharmaceuticals. Therefore, applying appropriate excipients to preserve their stability becomes essential. Therapeutic proteins, including antibodies and antibody–drug conjugates, made their way to the market by having the first antibody–drug (muromonab-CD3 (Orthoclone OKT3, Janssen-Cilag)) approved by the Food and Drug Administration (FDA) in 1986. Since then, many antibody-based drugs have been approved and commercialized (Kim et al. 2016a , b ; Singh et al. 2018 ). Given that their stability during the manufacturing process and their storage are of utmost importance and the fact that any single mAb requires its optimal production process parameters, e.g., excipients' type, combination, and concentration (Emami et al. 2018a , b ; Emami et al. 2019 ) (Fig.  1 ). Emami et al. constructed spray freeze-dried IgG microparticles using different amino acids including Leu, Phe, Arg, Gly, and cysteine (Cys) in the presence of trehalose to investigate the effect of the amino acids on the stability of IgG through SFD method. Pure spray freeze-dried-IgG resulted in the formation of 14% of IgG aggregates, however; IgG formulations stabilized using Leu, Phe, or Gly in the presence of trehalose have demonstrated aggregates < 2.2%. Combination of Phe and trehalose was most effective in stabilizing IgG against different verities of stresses during SFD. Arg and Cys were destabilizers representing aggregation and fragmentation of IgG, respectively. The IgG formulations prepared with Leu, Phe, or Gly in the presence of trehalose showed good stability (40 °C and 75% relative humidity for two months). Thus, a combination of the trehalose and uncharged, nonpolar amino acids have demonstrated the most stabilizing effects for spray freeze-dried-IgG formulations (Emami et al. 2018a , b ). In another study by Milani and colleagues, hydroxypropyl beta-cyclodextrin (HPβCD), renowned for its water-replacement, vitrification, and surfactant-like effects, was added to IgG formulations along with trehalose in different ratios ranging from the upper and lower ratios of 1:2 and 1:0.05 IgG: HpβCD, respectively. Among combinations with varying ratios, two formulations with the following ratios 1:2:0.25 (IgG: trehalose: HPβCD) and 1:2:0.05 had the minimum aggregation constants (0.46 ± 0.02 and 0.58 ± 0.01, respectively) after one month of storage at 45 °C and 60% of relative humidity. Measuring induced soluble aggregates after SFD and 1 and 2 months post SFD showed intriguing results as follows: all formulations' aggregations ranged between 0.01% and 0.1%, with a 1:2:2 ratio hitting the minuscule amount (0.01%), 0.25 ± 0.05 and 0.28 ± 0.02% of aggregation reported as the lowest levels belonging to 1:2:0.25, 1:2:0.05 in 2 months storage post SFD. Tracking chemical degradation in all samples after storage revealed no visible fragments of IgG molecules. The percentage of the dominant secondary structure of IgG molecules, beta-sheet structure, ranged between 65.13% and 77.82% following SFD. Beta-sheet content after storage conditions were slightly higher (66.32–78.15%). Finally, FPF and ED were measured as representatives of formulations' aerosol performance. For chosen formulations, 1:2:0.25 and 1:2:0.05 ratios, FPF values were 56.43 and 48.12%, respectively and their respective ED values were 93.15 and 91.23% (Milani et al. 2020 ). Supercritical fluid drying (SCFD) Among various existing drying methods spoken of so far, SCFD technique is an intriguing one due to its unique features, including being non-toxic, non-flammable, inert, recyclable, and readily removable by reducing the pressure (Costa et al. 2021 ) and being ecofriendly (Xu et al. 2018 ) and applying supercritical carbon dioxide (scCO 2 ) as a benign solvent to process polymers under such harsh conditions (temperature: 31.1 °C, pressure: 73.8 bar). This technology's feasibility in producing polymer-based porous microparticles with a minimum amount of residual organic solvent is noticeable (Xu et al. 2018 ). With solvent remnants in the product, storage stability and drug administration could be compromised (Park et al. 2019 ). Moreover, particle morphology is a subject under control through this process, and uniformed particle size is also achievable (Kankala et al. 2018 ). Based on applying scCO 2 , various drying techniques are available such as rapid expansion of supercritical solvent (RESS), particle from gas saturated solution (PGSS), carbon dioxide-assisted nebulization with a bubble dryer (CAN-BD), supercritical assisted atomization (SAA)/ supercritical CO 2 assisted spray drying (SASD), depressurization of an expanded liquid organic solution (DELOS) and supercritical CO 2 as anti-solvent. Regarding the biological products, the gas anti-solvent method is the most popular among other methods based on supercritical drying (Wilson et al. 2018 ). In one study, Wu et al. fabricated HPβCD particles by employing scCO 2 as the spraying medium and ethanol as the solvent in the supercritical assisted atomization (SAA) process. They aimed to investigate the effects of ethanol as the solvent on morphology and the size of inhalable particles and to optimize the involved parameters of SAA in producing those particles. Moreover, their formulations were entirely designed by adding the proper amount of Leu as an ingredient known to affect dry powders' aerosol performance positively. In their study, several parameters including solvent's and HPβCD solution's concentrations (W/W), precipitator and saturator temperatures, and the flow rate ratio of CO 2 /HPβCD were investigated. In addition to eighteen tests run for determining the most practical value among all varying ones, six tests were run to determine the effect of different concentration of Leu. Measuring particle size showed that enhanced ethanol concentration resulted in more atomization and reduced particle size. Notably, adding ethanol to the binary mixture of water and CO 2 increased CO 2 solubility by nine-fold. Despite the positive effect of increased ethanol concentration on micronization, its undesired effect on the shape is noticeable. In order to avoid irregular or shell particles and benefit from micronization, the ethanol concentration of 54.2% (w/w%) was chosen. Other optimal parameters were reported as precipitator (T P ) and saturator (T s ) temperatures of 373.2 K and 353.2 K, respectively. Following set optimal parameters of SAA process T P : 373.2 K, T s : 353.2 K, flow ratio of CO 2 /HPβCD: 1.8, and fixed concentration of the HPβCD solution 10 mg/mL, Leu was added to investigate formulations' aerosol performance. The mass concentration of 13% achieved a FPF value of 27.8 ± 0.4. whereas the augmented concentration of Leu to 16.7% resulted in agglomerations and reduced FPF value (Wu et al. 2021 ). In another study conducted by Xu et al., the fabrication of nano-embedded porous microparticles (NEPMs) to deliver both multi-drug resistance protein 1 (MRP1) siRNA and doxorubicin (DOX) in order to overcome multi-drug resistance (MDR) observed in the lung cancer, e.g., small cell lung cancer, was reported. By using a supercritical antisolvent process (SAS) and CO 2 as an antisolvent in the process, they could encapsulate DOX and prefabricated siRNA-chitosan (siRNA-CS) nanoparticles into polymer-based, poly-L-lactide (PLLA) to form (siRNA-CS-DOX-PLLA PMs) considered as NEPMs. Characterization the physical properties of the siRNA-CS nanoparticles displayed spherical structures with a narrow size distribution, an average diameter of 100 nm, and loading efficiency of 77.4%, which is remarkable. These particles could sustainably release ~ 60% of siRNA in 24 h. The final microstructures were rough over the surface, indicating the excellent attachment of NPs, and highly porous having an average geometric particle size of 16.86 µm. Considering the reported aerodynamic properties of NEPM, increasing DOX content had no significant effect on measured values of D g or D a , yet all features were at an optimal level for pulmonary delivery (10 µm < D g , 1 < D a  < 5 µm, FPF > 50%). Visual observation of the NEPM's aerosolization behavior was achieved in 0.12 s post actuation, which is considered good mobility. Releasing 60% to 80% of the entrapped DOX from NEPMs took place as slowly as in 60 h. The subcellular localization of NEPMs in H69AR cancer cells was investigated as an indicator of their delivery efficiency. Based on the results, cellular uptake of siRNA-CS nanoparticles was high, and these nanoparticles mediated siRNA release was via the escape from the cytosol. Performing anticancer efficacy tests revealed that NEPMs had the strength to lower cell viability to ~ 46%, while the results of other formulations (DOX, DOX-PLLA PMs, and NC NEPMs) were > 80% (Xu et al. 2018 ). Promising drying techniques So far, several methods to produce dried powders of biopharmaceuticals have been discussed, yet there are other potential techniques worthy of being named at least. The particle replication in non-wetting templates (PRINT®) technology is a lithography-based method with the potential to precisely control the size and the shape of particles and their monodispersity (El-Hammadi et al. 2022 ) by adjusting mold dimensions (Shah et al. 2022 ). Applying PRINT technology makes the possibility to load a wide range of drugs from hydrophobic to hydrophilic ones. Produced poly-lactic-co-glycolic acid (PLGA) nanoparticles could be in the shape of a needle or a cylinder (El-Hammadi et al. 2022 ). This method has been applied to micro mold proteins into high-performance dry powders (Wilson et al. 2018 ) to synthetize lipid-polymer hybrid nanocarriers (Shah et al. 2022 ) for delivery of influenza vaccine antigens (Rana 2021 ). Another wide-spreading method is fluidized bed drying in which the drug incorporating solution gets sprayed onto the inert carrier beads in fluidized bed systems having hot gas. This method is usually of choice to formulate oral drug delivery systems of peptides (Vass et al. 2019 ) though its productions cover pharmaceutical and food powders to detergents and fertilizers (Orth et al. 2022 ). Accordingly, Tyagi et al. constructed a multi-unit particulate system with the purpose of targeted oral delivery of a glucagon like peptide-1 (GLP-1) agonist peptide. They used a fluidized bed system for drug layering, seal coating, sustained release coating, mucoadhesive and enteric coating (Tyagi et al. 2021 ). Other methods, namely vacuum drying, microwave drying, and electrospinning are drawing attention as they show potential for being more efficient drying methods than conventional ones (Sharma et al. 2021 ). Biopharmaceuticals in clinical trials The market of biopharmaceutical products consists of monoclonal antibodies, purified proteins, vaccines, cell and gene therapies, synthetic immunomodulators, and recombinant biomolecules i.e., growth factors, proteins, hormones, as well as enzymes. This market with such diversity has the potential to see a $534.19 billion revenue in 2027 with a compound growth rate of 7.32% over the years 2022 to 2027 (Intelligence 2022 ). Increasing interest for manufacturing these products comes from their higher efficacy in treating many diseases including chronic viral hepatitis, rheumatoid arthritis, psoriasis and some types of cancers. Since these molecules are large in weight and biologically instable, the usual administration route is parenteral and mostly in form of lyophilizates, diluted or concentrated solution and suspensions (Bjelošević et al. 2020 ). On the other hand, there are inhalable dried powders or solutions of biologic molecules, proteins, which are or were commercially available such as Pulomozyme®, Technosphere ™ Afrezza® and Exubera®. Moreover, many other products of this type have been undergoing clinical trials (Karimi et al. 2022 ). Table 1 . shows a number of biopharmaceutical products with FDA approval and biopharmaceuticals in clinical trials since 2018. However, Resusix® clinical trial was terminated (Entegrion 2020 ). Table 1 A list of FDA-approved and clinical trials studies of biopharmaceuticals Biological Brand/dosage form Condition or disease NCT No./STN Production method Excipients Route of administration References ALVAC-HIV (vCP2438) (Canarypox virus), BIVALENT SUBTYPE C (2 recombinant monomeric proteins mixed with MF59® adjuvant) NA/lyophilized vaccine HIV NCT02404311 Freeze drying NA Intramuscular National Institute of et al. ( 2018 ) Coagulation factor VIIa (recombinant)-jncw SevenFACT®/lyophilized powder Hemophilia A or B with inhibitors 125641 Freeze drying Arginine hydrocholoride, glycine, isoleucine, lysine hydrochloride, polysorbate 80, trisodium citrate dihydrate, hydrochloric acid and nitrogen IV FDA ( 2020 ) Glu-Plasminogen Ryplazim®/lyophilized powder Plasminogen deficiency type I 125659 Freeze drying sodium citrate, sodium chloride, glycine, and sucrose IV (FDA 2021 a) Levodopa INBRIJA®/inhalation powder Parkinson 209184 Spray drying dipalmitoyl-sn-glycero-3-phosphocholine (DPPC) and sodium chloride Inhalation FDA ( 2021 b), Sharma et al. ( 2021 ) Live, attenuated BCG (Bacillus Calmette-Guerin Strain) NA/lyophilized vaccine COVID-19 NCT04475302 Freeze drying NA Intradermal Tuberculosis Research Centre et al. ( 2021 ) LMN-101 NA/capsule Campylobacter Jejuni infection NCT04098263 Spray drying Spirulina biomass Orally Lumen Bioscience ( 2020 ) NTD-RBD derived from S protein of Omicron variant (RH109) NA/lyophilized mRNA vaccine COVID-19 NCT05366296 Freeze drying ALC-0315 (4- hydroxy butyl) azanediyl) bis (hexane-6,1-diyl) bis (2- hexyldecanoate), ALC-0159 (2- [(polyethylene glycol)-2000]-N, N-ditetradecylacetamide), DSPC [1,2- distearoyl-sn-glycero-3-phosphocholine], Cholesterol, Trometamol and Sucrose Intramuscular Wuhan Recogen Biotechnology Co ( 2022 ) Recombinant human coagulation Factor VIIa (rFVIIa) NOVOSEVEN® RT/ lyophilized powder Congenital Hemophilia A or B with Inhibitors, Acquired Hemophilia, Congenital Factor VII Deficiency, Glanzmann’s Thrombasthenia 103665 Freeze drying Sodium chloride, calcium chloride dihydrate, glycylglycine, poly dorbate80, mannitol, sucrose, methionine Intravenous FDA ( 2014 ), Nordisc ( 2021 ) Resusix® (solvent/detergent treated plasma), FP24 (frozen plasma) Resusix®/NA Acquired coagulopathy NCT03700723 Spray drying NA Intravenous Entegrion ( 2020 ) Triptorelin pamoate Trelstar ® LA/suspension for injection Advanced prostate cancer NA Spray drying PLGA, mannitol, carboxymethycellulose sodium, polysorbate 80 Intramuscular Sharma et al. ( 2021 ) Resusix® clinical trial was terminated NTD-RBD N-terminal domain, receptor binding domain, HIV human immunodeficiency virus, MF59® an oil-in-water emulsion as adjuvant Characterization of dried-powder proteins The critical aspect to the success of therapeutic proteins involves improved methods to evaluate the processed particles and characterize these proteins. Characterization tests include physical powder characteristics, in vitro aerosol performance, and physicochemical stability tests of dried powders. Furthermore, for therapeutic proteins, the conformational stability and biological activity of dried active pharmaceutical ingredients (APIs) are required (Wanning et al. 2015 ) (Fig.  1 ). Solid powder characteristics Processed particles by different drying techniques have shown various sizes and morphologies. Powder characteristics have been categorized based on the required administration route of APIs, including parenteral, pulmonary, nasal, and epidermal drug delivery systems (Wanning et al. 2015 ). The analytical methods used to evaluate powders' physical characteristics are summarized in Table 2 . A successfully dried powder inhalation has good powder dispersibility, influenced by powder characteristics. The formulation, particle size, bulk density, specific surface area, and flow properties should be considered to have a proper aerodynamic behavior of the processed powders (Maa et al. 1999 ). Table 2 Analytical techniques for physical powder characteristics Analytical methods Principles Consideration Proteins & peptides References SEM, TEM Size, Surface structure, Morphology Solid IgG, Lysozyme, Anti-IgE Mab, rhDNase, PTH, Anthrax vaccine, Influenza vaccine Sarciaux et al. ( 1999 ), Jovanovic et al. ( 2008a , b ), Ramezani et al. ( 2013 ), Faghihi et al. ( 2014 ), Emami et al. ( 2018a , b ), (Jovanovic et al. ( 2006 ), Jovanovic et al. ( 2008a , b ), Nuchuchua et al. ( 2014 ), (Maa et al. ( 1999 ), (Poursina et al. 2015 ), (Wang et al. 2012 ), (Maa et al. 2004 ) BET Specific surface area IgG, Anti-IgE Mab, rhDNase (Jocelyn ( 1967 ), Awotwe-Otoo et al. ( 2015 ), Maa et al. ( 1999 ) DLS Hydrodynamic size (1–1000 nm) Liquid & Suspension, Spherical particles IgG Emami et al. ( 2018a , b ) SLS Size (1–1000 µm) Molecular weight Suspension IgG, Anti-IgE Mab, rhDNase, PTH, Anthrax vaccine, Influenza vaccine Ramezani et al. ( 2013 ), Faghihi et al. ( 2014 ), Emami et al. ( 2018a , b ), Maa et al. ( 1999 ), Poursina et al. ( 2015 ), Wang et al. ( 2012 ), Maa et al. ( 2004 ) Flow imaging microscopy Size (1–500 µm), Porosity IgG, Lysozyme Nuchuchua et al. ( 2014 ) NTA Concentration, Arithmetic size (30–1000 nm) IgG, Lysozyme Nuchuchua et al. ( 2014 ) Karl- Fischer Residual moisture IgG, Lysozyme, Anti-IgE Mab, rhDNase, IFN-α-2a, Anthrax vaccine, BSA Sarciaux et al. ( 1999 ), Ramezani et al. ( 2013 ), Awotwe-Otoo et al. ( 2015 ), Garidel et al. ( 2015 ), Jovanovic et al. ( 2006 ), Jovanovic et al. ( 2008a , b ), Nuchuchua et al. ( 2014 ), Maa et al. ( 1999 ), Kumar et al. ( 2009 ), Wang et al. ( 2012 ), Imamura et al. ( 2003 ) TGA Residual moisture Lysozyme Liao et al. ( 2004 ) Dynamic vapor sorption Relative humidity (Hygroscopicity) Solid Influenza vaccine Saluja et al. ( 2010 ) MDSC solid & liquid state Crystallinity, Glass transition Solid & liquid IgG, Lysozyme, Etanercept, Anthrax vaccine, BSA Vermeer et al. ( 2000 ), Jovanovic et al. ( 2008a , b ), Sahin et al. ( 2010 ), Awotwe-Otoo et al. ( 2015 ), Jovanovic et al. ( 2006 ), Jovanovic et al. ( 2008a , b ), Nuchuchua et al. ( 2014 ), Kim et al. ( 2014 ), Kim et al. ( 2016a , b ), Wang et al. ( 2012 ), Imamura et al. ( 2003 ) X-ray diffraction Crystallinity Solid IgG, Lysozyme Jovanovic et al. ( 2008a , b ), Faghihi et al. ( 2014 ), Emami et al. ( 2018a , b ), Jovanovic et al. ( 2006 ), Jovanovic et al. ( 2008a , b ) Andersen-cascade impactor, Multi-stage impinge, Twin stage impinge, Next generation impactor Aerodynamic behavior (FPF, Span) Solid IgG, Growth hormone, Anti-IgE Mab, rhDNase, Alkaline phosphatase, Adalimumab Faghihi et al. ( 2014 ), Kim et al. ( 2016a , b ), Maa et al. ( 1999 ), Li et al. ( 2010 ), Emami et al. ( 2019 ), Kim and Kim ( 2016 )  SEM scanning electron microscopy, TEM transmission electron microscopy, BET Brunauer–Emmett–Teller, DLS dynamic light scattering, SLS static light scattering, NTA Nanoparticle tracking analysis, TGA thermogravimetric analysis, MDSC modulated differential scanning calorimetry, PTH parathyroid hormone, BSA bovine serum albumin, IFN-α-2a interferon-alpha-2a The surface morphology of the processed powders was evaluated by using electron microscopy. The most important electron microscopy techniques for powder analysis are scanning electron microscopy (SEM) and transmission electron microscopy (TEM). TEM and SEM methods were applied to evaluate the particles in the range of 1–10 µm (Merkus 2009 ). Both microscopic methods have high resolution, enabling detailed information about the particle structure. However, due to the limited photo area in the millimeter range, information about the particle morphologies is not representative of whole samples. SEM represents three-dimensional images of the surface of particles as well as particle porosity (Zolls et al. 2012 ). However, TEM micrographs have been performed to show the outer shell and internal structure of processed particles to assess porosity and drug loading. The content distribution of particles was evaluated by TEM (Chen et al. 2012 ). The surface area is vital in the absorption of APIs in the pulmonary drug delivery system. Also, powder surface area has influenced the degradation of protein formulations during freezing and crystallization (Awotwe-Otoo et al. 2015 ). Brunauer–Emmett–Teller (BET) method determines the specific surface area per unit weight of dried particles by adsorption nitrogen gas (Maa et al. 1999 ). Liquid nitrogen is adsorbed as a monolayer on the surface of microparticles. Increasing the pressure pores at the surface of particles are filled with liquid nitrogen. Specific surface areas are estimated by considering the pressure fluctuation (Filipe et al. 2013 ). Specific surface areas was shown for IgG, which determines how the freezing rate affects the size and surface area of final freeze dried powders (Table 2 ) (Sarciaux et al. 1999 ; Awotwe-Otoo et al. 2015 ). A laser diffraction analyzer (static light scattering) measured the particle size distribution of the processed powders in a liquid suspension (Maa et al. 1999 ). Particle size analysis was performed to size subvisible particles larger than 1 µm up to 1 mm (Hawe et al. 2009 ). The particle size measurement is based on the light scattering intensity. Protein formulation for pulmonary drug delivery must have an aerodynamic diameter of 1–5 μm. Poursina et al. prepared a parathyroid hormone (PTH) formulation for inhalation with a geometric size of 14–16 µm. However, because of the low density of porous particles processed by SFD, these peptide particles have the proper aerodynamic diameter for inhalation (Poursina et al. 2015 ). On the other hand, dynamic light scattering (DLS) can determine particle size in the range of 1–10 µm. DLS, based on the diffusion of particles in solution, can measure intensity changes of laser light scattered by the sample. Hydrodynamic diameter is determined according to the diffusion coefficient of solutes in an aqueous solution. In DLS, because of the hydrodynamic layer, the measured particle size is larger than the size determined by TEM (Gaumet et al. 2008 ). Flow imaging microscopy measures particle size without any isolation. The particles pass through an imaging field, which is lightened by a light source and imaged by a charge coupled device camera. Automated image analysis can determine the morphology, particles size, and concentration (Zolls et al. 2012 ). Nanoparticle tracking analysis (NTA) is another method to measure the size and concentration of nanoparticles. NTA is a combination of laser light-scattering microscopy with a charge coupled device camera. NTA, in comparison to DLS, has peaks with higher separation capacity. In addition, information about the concentration and heterogeneity of particles by visualization is available. NTA and DLS can determine the aggregate percentage in solutions (Zolls et al. 2012 ). After the drying procedure, the residual moisture content of dried protein powders was determined with a Karl-Fischer titrator. The Karl Fischer coulometer determines the sample's water content based on an iodine/iodide redox reaction, in which the remaining water in the protein sample reacts with iodine until all water is consumed (Garidel et al. 2015 ). The remaining water probably results from bound, free or bulk water in dried powder based on the protein product. Generally, based on Food and Drugs regulations, the maximum residual moisture content should be equal to or less than 3% to maintain the protein stability (Nuchuchua et al. 2014 ). The hygroscopicity of the powders was determined by dynamic vapor sorption (DVS). In the gravimetric sorption analyzer, the powders were subjected to 0–70% relative humidity at room temperature, and the weight change equal to water uptake was determined (Saluja et al. 2010 ). Modulated differential scanning calorimetry (MDSC) by scanning different protein formulations has the potential to detect whether there are interactions between proteins and excipients at the molecular level or not (Tian et al. 2006 ). Also, the thermal behavior of dried protein formulation compared to the physical mixture or individual excipients and proteins was evaluated. The melting or crystallization transition in a protein formulation thermogram confirms the product's crystallinity, which is not preferable, and vice versa (Nuchuchua et al. 2017 ). The glass transition values and melting points for different solid formulations were determined using a differential scanning calorimetry (DSC) device. DSC was accomplished on powder samples. Typical glass transition peaks for SFD formulations of vaccine were not detected in all formulations scans due to interference from other thermal transitions (Wang et al. 2012 ). On the other hand, the Nano DSC can be done for liquid protein formulations to evaluate the structural stability of the protein (Kim et al. 2016a , b ). Crystallinity is determined by X-Ray diffraction (XRD). XRD technique is applied to study the solid states of solutes in frozen aqueous solutions (Oetjen 2004 ). For the crystalline combination, a sharp peak appeared. However, the formulation in an amorphous state does not have a sharp peak. Amorphous protein/excipients because of better solubility and improved stability are desirable. Faghihi et al. prepared stable spray-dried IgG with Leu. However, the antibody has shown some aggregates in the presence of Gly that has a crystalline structure (Faghihi et al. 2014 ). The aerodynamic behavior is important to have a successful inhalable dried powder, which influences drug deposition for inhalation (Ali et al. 2014 ). The dry powder's aerosol performance was evaluated using twin stage impinger, multi-stage liquid impinger, Anderson-cascade impactor (ACI), and the Next-generation impactor (NGI) (Wanning et al. 2015 ; Emami et al. 2019 ). Amounts of powders collected from different stages of these devices were determined, representing the aerodynamic particle size. Using these devices, we can estimate by inhalation how much the drug will reach the alveolar airways (Maa et al. 1999 ). A cascade impactor measures the particle size as it distributes via an opening with the use of aerosol. The ACI, manufactured by Copley, can predict the deposition profile of aerosol particles into different parts of airways respiratory system. ACI with eight collection plates and a filter stage has been designed for measuring the aerodynamic particle size distributed by dry-powder inhalers (DPIs) and metered-dose inhalers (MDIs) (Newton et al. 1977 ; Yoshida et al. 2017 ; Dechraksa et al. 2020 ). While the NGI is a high-performance cascade impactor with seven collection cups and different cut-off diameters for classifying aerosol particle into size fractions for testing MDIs and DPIs and other inhaled drug delivery devices including nasal sprays and nebulizers (Marple et al. 2003 , 2004 ; Yoshida et al. 2017 ). The schematic figures of the impactors and some of their features are displayed in Fig.  3 . Fig. 3 The schematic figure displays two impactors, Andersen cascade impactor (ACI) and Next generation impactor (NGI) as well as their features Conformational stability Due to the delicate nature of protein structure, secondary or tertiary structure of proteins are susceptible to changes during drying methods. Detection of variation in protein's secondary or tertiary structure can be challenging, especially if they involve only a tiny part of the therapeutic protein (Houde et al. 2014 ). Some examples of spectroscopy methods for particles engineered by different drying procedures are available (Table 3 ). Table 3 Analytical methods for evaluating the protein conformation Spectroscopy methods Principle Detection Properties Proteins & peptides Reference Far CD, Near CD, Spectroscopy Aromatic amino acid environment, Peptide bond Secondary structure, Tertiary structure, Quaternary structure Fairly expensive, Liquid sample IgG, Lysozyme, Etanercept, PTH, Anthrax vaccine Vermeer et al. ( 2000 ), Schüle et al. ( 2007 ), Hawe et al. ( 2009 ), Sahin et al. ( 2010 ), Emami et al. ( 2018a , b ), Jovanovic et al. ( 2006 ), Nuchuchua et al. ( 2014 ), Kim et al. ( 2014 ), Poursina et al. ( 2015 ), Wang et al. ( 2012 ) FTIR Peptide bond structure Secondary structure Cheap solid and liquid sample IgG, Lysozyme, Etanercept, BSA, Anthrax vaccine Schüle et al. ( 2007 ), Hawe et al. ( 2009 ), Awotwe-Otoo et al. ( 2015 ), Jovanovic et al. ( 2008a , b ), Kim et al. ( 2014 ), Kim et al. ( 2016a , b ), Imamura et al. ( 2003 ), Wang et al. ( 2012 ) Fluorescence, Spectroscopy (Intrinsic & Extrinsic) Aromatic amino acid environment Tertiary structure, Quaternary structure Liquid sample IgG, PTH, Lysozyme Hawe et al. ( 2009 ), Sahin et al. ( 2010 ), Emami et al. ( 2018a , b ), Poursina et al. ( 2015 ), Jovanovic et al. ( 2006 ) UV absorbance spectroscopy Aromatic amino acid environment Tertiary structure Cheap liquid sample IgG Emami et al. ( 2018a , b ) CD circular dichroism, FTIR fourier transforms infrared, BSA bovine serum albumin In order to study the structure of processed proteins in the solid-state, Fourier transforms infrared (FTIR) spectroscopy is applied (Jovanovic et al. 2008a , b ). FTIR spectra estimate the secondary structure elements in the solid-state. Each protein has a unique spectrum and the significant peaks in the second derivatives spectra are found, which are related to α-helix, β-sheet, turn, and a random coil of the protein structure (Schüle et al. 2007 ). After reconstitution, the protein conformation was further investigated using circular dichroism (CD) and fluorescence spectroscopy to determine whether the protein preserved its structure (Jovanovic et al. 2008a , b ). CD is a valuable spectroscopy technique for evaluating the structure of proteins in solution. By absorption of radiation, CD signals appear, and spectral bands are related to distinct structural characteristics of a protein. From the intensity of spectral regions, complementary protein structural information can be provided (Kelly et al. 2005 ). Far-UV CD region with wavelength ranging from 190 to 250 nm, related to the peptide bond absorption and information on the protein secondary structure can be obtained. However, the near-UV CD chromophore, a wavelength range between 250 and 320 nm, reflects the aromatic amino acid residue and therefore gets information about the tertiary structure of a protein (Hawe et al. 2009 ) and broad absorption peaks with less intensity centered at 260 nm belong to disulfide bridges (Kelly et al. 2005 ). CD spectroscopy is suitable for determining whether a protein is folded, determining the percent of α-helix, β-sheet turns, and random structure in proteins, and comparing the secondary structure of proteins in different conditions, including temperature, pH, salt, protein concentration, ligands, etc. Also, CD spectroscopy is applied to measure the protein stability via thermal melts and denaturation studies, testing the structural integrity of site-directed mutations and the stability of domain structures (Kelly et al. 2005 ). Fluorescence spectroscopy is a highly sensitive method for evaluating the conformation of the protein. Intrinsic protein fluorescence spectra are derivatives of the fluorescent amino acid, tryptophan, and tyrosine, which can provide information on changes in protein structure. On the other hand, extrinsic fluorescent dyes like 1-anilinonaphthalene-8-sulfonate (ANS), Bis-ANS, Nile Red, Thioflavin T, Congo Red can produce covalent linkage to proteins, e.g. via the ɛ-amino group of lysine, the α-amino group of the N-terminus, or the thiol group of cysteine and so on they perform protein analysis (Hawe et al. 2008 ). Although CD and FTIR spectroscopy has high sensitivity with high resolution, Ultra-Violet (UV) absorption spectroscopy has gained attraction to study the protein conformational changes. UV absorbance as a zero-order or derivative analysis is a rapid, nondestructive, high resolution, and cheap alternative to other commonly used spectroscopic techniques for protein analysis (Engineers et al. 2003 ). Nano DSC is a highly sensitive DSC with high-resolution to investigate the thermal stability of large biopharmaceuticals in liquid samples. The Nano DSC have a potential to characterize the thermal stability of their samples without the use of exogenous tags or dyes, thereby simplifying workflows with higher accuracy and more reproducibility. The Nano DSC determines the heat of reaction from tertiary and secondary structure changes that occur when a biomolecule unfolds. In addition, this instrument in one experimental set up, can measure the enthalpy, melting temperature, heat capacity, and calculate the free energy to evaluate the stability of sample (Spink 2008 ; Gill et al. 2010 ). Physicochemical stability Despite the attractiveness of different drying procedures, these processes generate a variety of freezing and dehydration stresses which are destructive for protein formulations (Tian et al. 2006 ). Because of complexity, variation of protein instability, and presence of aggregates with extended particle size range, more than one physicochemical technique was desired to characterize the instability (Table 4 ) (Houde et al. 2014 ). DLS, or quasi-elastic light scattering or photon correlation spectroscopy, is used to determine the hydrodynamic size of innate proteins (Zolls et al. 2012 ). In addition, DLS is highly sensitive method to detect dimers and large aggregates in the size ranging between 1 nm and 10 µm (Hawe et al. 2009 ; Emami et al. 2018a , b ). In size exclusion chromatography (SEC), proteins are separated based on their hydrodynamic size. Generally, SEC is performed to identify and quantify protein monomers, fragments, and small aggregates. In SEC, the percent of soluble aggregates can be estimated by directly the peak area of aggregates and for insoluble aggregates as a loss area in the total peak area. UV absorbance, fluorescence, or refractive index are typical detectors for evaluating protein content. Light scattering detectors can estimate the molecular weight of the monomer and aggregates (Zolls et al. 2012 ; Emami et al. 2018a , b ). Usually, SEC result has high precision; however, the nonspecific interaction of proteins and protein oligomers in the chromatography columns are existed (Engineers et al. 2003 ). Table 4 Analytical techniques for physicochemical characterization of protein Methods Principles Instability Applications Proteins & peptides Reference DLS Hydrodynamic size, Polydispersity Physical Aggregation (1 nm–10 µm) IgG, Etanercept Sarciaux et al. ( 1999 ), Ahrer et al. ( 2006 ), Hawe et al. ( 2009 ), Menzen et al. ( 2014 ), Emami et al. ( 2018a , b ), Kim et al. ( 2014 ), Kim et al. ( 2016a , b ) NTA Concentration, Arithmetic size Physical Aggregation (30–1000 nm) IgG, Lysozyme Nuchuchua et al. ( 2014 ) SLS (Light Obscuration) Average Mw Physical Aggregation (1–600 µm) IgG Hawe et al. ( 2009 ), Emami et al. ( 2018a , b ) Turbidity Optical density (λ ˃340 nm), Aggregation index Physical Aggregation IgG, Lysozyme Sarciaux et al. ( 1999 ), Ahrer et al. ( 2004 ), Jovanovic et al. ( 2008a , b ), Hawe et al. ( 2009 ), Menzen et al. ( 2014 ), Jovanovic et al. ( 2006 ), Jovanovic et al. ( 2008a , b ) SEC Hydrodynamic size, Mw Chemical, Physical Fragmentation, (Disulfide) oxidation, Aggregation, dimer (1–100 nm) IgG, Lysozyme, Etanercept Sarciaux et al. ( 1999 ), Ahrer et al. ( 2004 ), Schüle et al. ( 2007 ), Sahin et al. ( 2010 ), Garidel et al. ( 2015 ), Emami et al. ( 2018a , b ), Nuchuchua et al. ( 2014 ), Kim et al. ( 2014 ), Kim et al. ( 2016a , b ) IEX Charge Chemical Deamidation ((1–100 nm) IgG Wang et al. ( 2007 ) RP-HPLC Hydrophobicity Chemical Fragmentation, Deamidation, (Disulfide) Oxidation (1–100 nm) Growth hormone Kim et al. ( 2014 ), Kim et al. ( 2016a , b ) Analytical Ultracentrifuge Mw Physical Aggregation – Jiskoot et al. ( 2005 ) Electrophoresis, Native-PAGE, SDS-PAGE, CE-SDS, MCGE Mw, Charge Chemical, Physical (Disulfide) oxidation, Fragmentation aggregation, Dimer, Isomerization IgG, Phosphopeptide, Lysozyme, Anthrax vaccine, Influenza vaccine, Adalimumab Alexander et al. ( 1995 ), Hawe et al. ( 2009 ), Awotwe-Otoo et al. ( 2015 ), Wang et al. ( 2015 ), Emami et al. ( 2018a , b ), Ollikainen et al. ( 2016 ), Wang et al. ( 2007 ), Jovanovic et al. ( 2006 ), Wang et al. ( 2012 ), Maa et al. ( 2004 ), Emami et al. ( 2019 ) LC–MS Mass Chemical Deamidation β-Lactoglobulins Monaci et al. ( 2007 ) Mass spectrometry, MALDI-TOF, ESI-TOF Mass/Charge Chemical, Physical Fragmentation, Low Mw aggregation IgG, Adalimumab Alexander et al. ( 1995 ), Sandra et al. ( 2014 ), Zhang et al. ( 2014 ), Emami et al. ( 2019 ) DLS dynamic light scattering, SLS static light scattering, NTA nanoparticle tracking analysis, IEX ion exchange chromatography, SEC size exclusion chromatography, RP-HPLC reverse phase- high performance liquid chromatography, Native-PAGE native polyacrylamide gel electrophoresis, SDS-PAGE sodium dodecyl sulfate polyacrylamide gel electrophoresis, CE-SDS capillary electrophoresis sodium dodecyl sulfate, MCGE microchip capillary gel electrophoresis, Mw molecular weigth, LC–MS liquid chromatography-mass spectrometry, MALDI-TOF matrix-assisted laser desorption/ionization-time of flight, ESI-TOF time-of-flight mass analyzer with an electrospray ionization Other chromatographic methods like reverse-phase-high-performance liquid chromatography (RP-HPLC) can recognize the chemical instability that caused hydrophobicity changes, including deamidatin, oxidation of disulfide bridge, β-elimination and isomerization of aspartic acid. On the other hand, ion-exchange chromatography (IEX) can separate with the principle of charge variation. In chemical reactions such as deamidation and β-elimination total charge of the degradation product is changed, which can be assessed by IEX method (Filipe et al. 2013 ). UV absorbance spectrum in wavelength between 240 to 350 nm is an alternative method to evaluate the aggregates. The aggregation index (AI) was estimated from optical densities (OD) in different wavelengths as OD340/(OD280-OD340) × 100. Protein aggregates, compared to native protein due to the higher light scattering, can cause increased turbidity at 340 nm wavelength. Therefore, AI is a good indicator for aggregate monitoring, which none of the intrinsic chromophores in protein structure absorb at this wavelength. AI values below 10 often indicate solutions with minor amounts of soluble aggregation (Emami et al. 2018a , b ). Sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE) is a conventional technique to determine the molecular weight of proteins and protein aggregates and fragments (Filipe et al. 2013 ). The principle of separation in SDS–PAGE is the relative molecular size in the presence of SDS (Park et al. 2010 ). SDS-PAGE under reducing and non-reducing conditions was carried out to distinguish whether the protein aggregates were composed of covalently or non-covalently linked monomers (Hawe et al. 2009 ). For protein quantification capillary electrophoresis sodium dodecyl sulfate (CE-SDS) is an alternative method. CE-SDS, because of its high resolution, has received significant attention. However, this electrophoresis method was still time-consuming in sample preparation with low sensitivity (Park et al. 2010 ). Microchip capillary gel electrophoresis (MCGE) is based on Lab-on-a-chip technology and is recognized as a high-performance analytical method. Among the electrophoresis techniques, MCGE, because of its high precision and high sensitivity detector with laser-induced fluorescence, is preferable. Furthermore, MCGE is automated with fast sample analysis (10 samples within 25 min) and a minimum amount of protein (4 µL of protein sample) (Park et al. 2010 ; Park et al. 2015 ). Capillary isoelectric focusing (CIEF) is another electrophoresis method that can separate based on proteins' isoelectric points (pI). As two isoforms cannot separate based on their size and molecular weight, Na et al. have demonstrated that although mass spectrometry or SDS-PAGE cannot distinguish between two isoforms, CIEF can discriminate ricin isoform very well (Na et al. 2011 ). Among analytical tools, mass spectrometry is a powerful option for assessing the physicochemical degradation of proteins. However, this method has limitation in the nature and concentration of additives and requires complex sample preparation for analysis. So, liquid chromatography- mass spectrometry (LC–MS) is a combination of chromatography and mass spectrometry which is a good alternative (Filipe et al. 2013 ). The liquid chromatographic method with electrospray ionization tandem mass spectrometry is a fast analytical method with high selectivity and sensitivity for quantification (Ji et al. 2011 ). Park et al. used developed liquid chromatography–tandem mass spectrometry to evaluate the stability of collagen pentapeptide, a subfragment of collagen with high precision and high accuracy (Park et al. 2012 ). Biological stability Each therapeutic protein or peptide after administration to patients has some efficacy associated with the biological activity of these drugs. Whenever the protein formulation is dried and formulated through a stressful procedure, it is critical to monitor the protein activity compared to unprocessed APIs. Potency assessment can be done by in-vitro and in-vivo tests to confirm the pharmacological efficacy of biologics is preserved significantly (Nuchuchua et al. 2017 ). Ramezani et al. prepared spray-dried trastuzumab and treated the human breast cancer cell line SKBr3, which confirmed that the bioactivity of the antibody was preserved after processing by SD (Ramezani et al. 2014 ). Local and systemic delivery of dried-powder biopharmaceuticals Respiratory diseases, asthma, chronic obstructive pulmonary disease (COPD) and lung cancer, as well as respiratory infectious diseases, pneumonia and tuberculosis (TB), have always been a serious issue to human’s society, not only threatening their lives but also negatively affecting their socioeconomic status (Parray et al. 2021 ). In the group of viral pathogens, we see corona virus, adenovirus, respiratory syncytial virus, influenza virus, rhinovirus, and measles, which are responsible for viral pneumonia (He et al. 2022 ). With the aim of treating either infectious respiratory diseases or systemic disorders, inhaled therapeutics reduce both applied dose and cost of therapy with benefiting patients to administer drugs individually or at a nursing home (Parray et al. 2021 ). Oligopeptides, cytokines, enzymes, vaccines, mAbs, genes and clotting factors are categorized as biopharmaceuticals (Osman et al. 2018 ). Pulmonary delivery of biopharmaceutics could be promising for preparing higher bioavailability than other routes while delivering lower dose of therapeutics (He et al. 2022 ). Local pulmonary system provides a rapid onset of action when it comes to low molecular weight drugs (Faghihi et al. 2021 ). Moreover, the efficacy of high molecular weight biomolecules due to the higher concentration of the biomolecules in respiratory organs is accelerated via inhalation. As in mAbs, it is reported that their accumulation in target organs, the lungs, is more when they are applied through inhalation. Therefore, other organs are less exposed to the therapeutic and related side effects such as toxicity and cytokine release syndrome are reduced (Parray et al. 2021 ). In addition, in terms of selectivity, protein biomolecules are superior to small drug molecules (Matthews et al. 2020 ). Although several trials in clinical and preclinical stages have been conducted, since 1993 the year in which Pulmozyme® was launched as an inhaled protein treatment for cystic fibrosis, no more such treatment has been introduced to the biopharmaceutical market (Matthews et al. 2020 ). Among many reported preclinical and clinical studies regarding local delivery of biomolecules as dried powders, infliximab as a mAb acting against TNF-α was utilized through respiratory system as a dry powder in Balbc/mice. According to results, secretion of TNF-α in mice’s lungs were remarkably reduced and resulted in locally inhibited inflammation (Faghihi et al. 2019 ). Clinically experimented inhaled proteins include anti-thymic stromal lymphopoietin (TSLP) antibody fragment (CSJ117), anti-interleukin (IL)-13 mAb fragment (VR942/CDP7766) (Liang et al. 2020 ) and a member of Anticalin® proteins acting as an IL-4Rα antagonist (AZD1402/PRS-060) all with efficacy against asthma (Matthews et al. 2020 ). Another clinical trial with focus on a rare autoimmune disease, pulmonary alveolar proteinosis, was conducted. The recombinant human granulocyte–macrophage colony-stimulating factor (GM-CSF) was inhaled as a lyophilized formulation by patients suffering from mild to moderate form of the disease. Laboratory findings showed a modest but significant change in alveolar–arterial oxygen gradient in the target group of patients (Tazawa et al. 2019 ). Aside from patients with respiratory disorders benefiting from local drug delivery through inhalation, those patients suffering from diseases including osteoporosis, diabetes, hormone deficiency and migraine (Keyhan shokouh et al. 2021 ) could enjoy the simplicity and non-invasiveness of such administration way (Dhahir et al. 2021 ). From a pharmacokinetic view, pulmonary delivery systems’ superiorities are large surface area (70–140 m 2 ), fast absorption and less enzymatic activity than oral route; it also bypasses first pass metabolism of the liver (Miyamoto et al. 2021 ). Hence, an enhancing number of preclinical and clinical studies are trying to bring more biomolecules from bench to bedside. Moreover, in some cases e.g., postpartum hemorrhage (PPH), inhalation could save many lives. Currently, oxytocin injections are applied to cease the hemorrhage. Oxytocin products require cold chain transport and storage, which are hardly affordable in low- and middle-income countries (Carvalho et al. 2020 ; Rahman et al. 2021 ). In order to address such urgent need for dried powders of oxytocin, devoid of cold supply chain, some of which have undergone preclinical (McArthur et al. 2017 ) and clinical trials (GlaxoSmithKline 2015 ; Fernando et al. 2017 ) to test their viability. A powder formulation with ultrafine size of oxytocin was developed by Prankered et. al. They used a postpartum sheep model to assess the efficiency of the spray-dried powder of oxytocin for in vivo evaluations. Results showed an onset of uterine electromyographic (EMG) activity after 129 ± 18 s post inhalation, which is noticeably shorter than 275 ± 22 s post intramuscular administration. Despite the difference in the onset of action, both EMG responses were similar and closely resembled the natural EMG activity following delivery. Noticeably, oxytocin formulation was well tolerated in the airway showing no irritability or distress (Prankerd et al. 2013 ). Myamoto and colleauges developed a dried powder formulation of another peptide, human Ghrelin (hGhrelin), which is responsible for enhancing hunger sensation. They aimed to change its administration from injection to inhalation. In this case, their powder achieved an FPF of 41.7 ± 3.8% and the bioavailability of optimum formulation tested in monkeys reached to a mark of 16.9 ± 2.6% (Miyamoto et al. 2021 ). Pulmonary delivery of peptides and proteins Due to the poor stability and limited permeability in gastrointestinal (GI), usually the parenteral administration of the therapeutic peptides and proteins are preferable (Zhu et al. 2021 ). Peptides and proteins have superior specificity due to highly selective receptor-binding that reduce off-target side effects (Osman et al. 2018 ). However, due to the high M W , hydrophilicity, instability, and subsequent limited absorption, therapeutic proteins and peptides have predominantly delivered through parenteral route. Short-circulatory half-life of peptides and proteins require frequent injections and subsequently lowering the patient compliance (Emami et al. 2018a , b ; Osman et al. 2018 ). Aerosolized peptide and protein due to the patient compliance, bypassing hepatic first pass metabolism, and avoidance of the harsh proteolytic GI environment could be an appropriate alternative for local or systemic delivery (Emami et al. 2018a , b ; Osman et al. 2018 ). Improved pharmacokinetics of peptide and protein due to rapid onset of action, the large surface area (100–140 m 2 ) of the lungs, and vascularized lung epithelium are amongst the inhaler benefits (Osman et al. 2018 ). Emami et al. investigated how the influence of different amino acids on the final formulation of adalimumab differs from one another in terms of the stability and aerosol performance. They processed adalimumab via SFD, benefiting from different types of amino acids including Leu, Phe, Gly, Arg, and trehalose in those formulations. All formulations, regardless of the type of the amino acids, showed highly porous and spherical particles. Regarding their size and size distribution, all amino acids-containing formulations showed small particles with a narrow span except for the Arg-containing formulation, which was not that satisfactory. Moreover, these stabilizers resulted in formulations in which the secondary structure of adalimumab was preserved. In term of stability, aggregation levels displayed how well amino acids stabilized adalimumab formulations during SFD, less than 4% aggregation, and under accelerated conditions (40 °C and 75% RH for three months), more than 95% intact adalimumab. In addition, data obtained from testing the biological activity of the formulations and their aerosol performance revealed more than 92% cell viability, comparable to the intact adalimumab, as well as FPF values of more than 50% with emitted dose (ED) figures more than 90%, excluding the Gly formulation (Emami et al. 2019 ). Quarta et al. synthetized the excipient-free of insulin formulation through SD procedure for post-prandial glucose control. Physico-chemical properties of spray-dried insulin was preserved within the storage (6 months at room temperature). In addition, spray-dried powder of insulin has shown the successful in vitro aerodynamic behavior. Pharmacodynamic as well as pharmacokinetics in rats that received intratracheal insufflation of spray-dried insulin powders were determined and compared with Afrezza inhalation insulin. Spray-dried insulin has shown the fast absorbance (t max 15 min and C max 4.9 ± 1.5 mU/mL) whereas, Afrezza had a slower absorption (t max 30 min and C max of 1.8 ± 0.37 mU/mL). After glucose injection, spray-dried insulin caused a sudden reduction of glucose level, similar to Afrezza. The subcutaneous injection of insulin due to the slow absorption, showed the prolonged insulin circulation level and consequently a long-lasting hypoglycemic efficacy (Quarta et al. 2020 ). Treatment efficacy against TB as an infectious respiratory disease, is enhanced via mucosal immunization induced by direct delivery of vaccines to the nose or lungs (Gomez et al. 2021 ). Gomez et al. constructed the thermostable formulation as an inhalable dry powder version of ID93 + GLA-SE, an adjuvanted subunit TB vaccine candidate, containing recombinant fusion protein ID93 and glucopyranosyl lipid A (GLA) in a squalene emulsion (SE) as an adjuvant system through SD procedure. Leu (20% w/w), trileucine (3%, 6% w/w), and pullulan (10%, 20% w/w) excipients in the presence of trehalose as a stabilizer was assessed. In the presence of Leu, the aerosol performance was enhanced, but induced aggregation of the emulsion droplets. Pullulan preserved emulsion droplet size; however, the antigen was not recognized after reconstitution. The trehalose-trileucine combination successfully stabilized the adjuvant system, with retention of the antigen, in an inhalable dry powder format for vaccine delivery (Gomez et al. 2021 ). Pulmonary delivery of siRNA Gene silencing specifically, short-interfering RNA (siRNA) through protein expression modification at the mRNA level by a sequence-specific posttranscriptional procedure known as RNA interference (RNAi) have a potential to inhibit the pathology pathways and introduce new treatment strategies for respiratory diseases (Ding et al. 2021 ; Zoulikha et al. 2021 ). The lung characteristics, including clear anatomy, accessibility, relative low enzyme activity, make a good target for local siRNAs therapy (Zoulikha et al. 2021 ). Inhalation-based delivery of siRNA for targeted delivery to specific lung cells holds great promise because it can reduce the overall dose required to treat pulmonary disorders in comparison to oral or parenteral routs. In addition, this reproducible and economical platform avoid first-pass metabolism, which reduce the dose and toxicity risk in diverse patient populations (Ding et al. 2021 ). In addition, siRNA as compared to other gene therapeutics, including the plasmid DNA (pDNA) and plasmid-based short RNAs (shRNA) could be easily constructed and avoids the gene therapy-related side effect (mutation and teratogenicity). Moreover, siRNA has a smaller size, higher transfection efficacy, potency and specificity, and lower immune response, making them the proper choice for RNAi therapeutics (Zoulikha et al. 2021 ). On the other hand, targeted delivery of siRNA to the lung due to the instability of naked siRNA molecules in systemic circulation and the negative charge of siRNA is challenging (Bardoliwala et al. 2019 ). Naked siRNA or different verities of siRNA-containing carriers including liposomes, dendrimers, polypeptides, micelles, inorganic nanoparticles (gold nanoparticles, silica nanoparticles), polymeric nanoparticles, and exosomes were applied for siRNA pulmonary delivery (Ding et al. 2021 ). Patisiran, the first approved siRNA therapy, stimulate the siRNA delivery to expand their scope of RNAi therapeutics to other diseases. Patisiran is a lipid nanoparticle containing the siRNA encapsulated with lipid excipients for delivery to hepatocytes. The nanoparticles are composed of ionizable cationic lipids (DLin-MC3-DMA), cholesterol, phospholipid (DSPC), and polyethylene glycol modified lipids (PEG2000-C-DMG). To enhance the physicochemical stability, the siRNA is modified with eleven 2′-methoxy-modified sugar residues and four 2′-deoxythymidine residues. GIVLAARI™ _(givosiran) is another RNAi medication for treatment of acute hepatic porphyria, which was approved in November 2019 (Ding et al. 2021 ). Miwata et al. have demonstrated that intratracheal administration of siRNA dry powder, vascular endothelial growth factor-specific siRNA (VEGFsiRNA), through the suppression of specific genes expressed in cancerous lung tissue was a successful therapeutic strategy for lung cancers. VEGFsiRNA inhaler was administered intratracheally to mice with metastatic lung cancers consisting of B16F10 melanoma cells or Lewis lung carcinoma cells. A single intratracheal dose of VEGF-siRNA diminished the VEGF expression levels in lung tumor tissue and bronchoalveolar lavage fluid. In addition, repeated intake of intratracheal VEGF-siRNA reduced the number of visible metastatic foci on the lung surface and tumor area in lung tissues (Miwata et al. 2018 ). Nasal delivery of vaccines In addition to the FDA-approved nasal vaccine, which is a liquid vaccine form, there is a growing interest in gel-based and dry powder vaccine formulations (Tai et al. 2022 ). Although liquid form of vaccines has limitations including the chemical, physical, and thermal instability, solid dosage form of vaccines have the advantages of improved physicochemical stability, which omit the role of preservatives and cold chain circulation (Wang et al. 2012 ; Tai et al. 2022 ). Different devices must be applied to actively deliver the dry powder vaccine into the nasal cavity. Until now, there is no FDA-approved dry powder vaccine for intranasal administration (Tai et al. 2022 ), but an increasing number of preclinical and clinical studies are undergoing to investigate new strategies for dry powder delivery of vaccines (Wang et al. 2012 ; Tai et al. 2022 ). Intranasal vaccination using dry powder vaccines is an attractive, non-invasive strategy with improved stability and enhanced protection at the mucosal surfaces (Thakkar et al. 2018 ). The immunization through injection usually fails to induce mucosal immunity or induce weaker immunity responses (Mato 2019 ). Nasal administration constitutes an alternative and promising strategy for vaccine delivery. Mucosal routes have several advantages supporting their selective use for different pathologies. Currently, many efforts are being made to develop effective drug formulations and novel devices for nasal delivery (Mato 2019 ). Thakkar et al. induced local and systemic immunity responses by intranasal immunization of a dry powder vaccine adjuvanted with an insoluble aluminum salt. The dry powder vaccine was prepared by thin-film FD of a model antigen, ovalbumin, adsorbed on an adjuvant (aluminum hydroxide). The dried vaccine have shown the proper aerodynamic behavior, good flow properties, and uniformly distribution of vaccine in dry powder. An in vitro nasal deposition study using nasal casts of humans showed that most of the dried powder was deposited in the nasal cavity (~ 90%). Intranasal immunization of rats with the dry powder vaccine stimulated a serum antibody response as well as specific IgA responses in the nose and lung secretions of the rats (Thakkar et al. 2018 ).

Conclusion In conclusion, using drying methods, protein formulations in the presence of stabilizers produce a solid dosage form with greater stability. Cryoprotectants and lyoprotectants maintain the stability and bioactivity of biopharmaceutical APIs. Based on the route of protein administration, a proper drying method was chosen, and the process parameters were optimized. Finally, formulation optimization was performed to determine the stable protein/stabilizer combinations. In addition, physical powder characterization and possible analytical technologies were employed to evaluate protein stability. Because each characterization test has strengths and limitations, a comprehensive analysis is required to recognize the cause of instability. Regarding the ongoing trend towards addressing current defects in biopharmaceutical production, searching for new drying methods as substitutes for conventional ones, and investigating novel excipients for more efficient stabilizing effects, these products could dominate the future pharmaceutical industry. Declarations Conflict of interest All authors (F. Emami, M. Keihan Shokooh, and S.J. Mostafavi Yazdi) declare that they have no conflict of interest. Research involving in human and animal participants This article does not contain any studies with human and animal subjects performed by any of the authors. Footnotes Publisher's Note Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations. Fakhrossadat Emami, Mahsa Keihan Shokooh, Seyed Jamaleddin Mostafavi Yazdi have equally contributed to this work. References Adali MB, Barresi AA, Boccardo G, Pisano R. 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# 干燥技术提高生物制药稳定性和递送效率的研究进展

## 摘要

**背景:** 大多数生物制药以液体制剂形式开发,其稳定性低于固体制剂。为确保生物制药的稳定性,在存在适当稳定赋形剂的情况下采用有效的干燥技术至关重要。可用于此目的的干燥技术多种多样,例如冷冻干燥或冻干法、喷雾干燥、喷雾冷冻干燥、超临界流体干燥、非润湿模板粒子复制技术以及流化床干燥。

**涵盖领域:** 本综述讨论了干燥技术及其在制备稳定的固态生物制药中的应用,提供了市售产品或临床试验制剂的实例。与此同时,我们还综述了如何利用不同的分析方法评估干燥蛋白质粉末的气溶胶性能和粉末特性。最后,我们从构象和理化稳定性以及生物活性方面评估了蛋白质的完整性。

**专家观点:** 吸入式生物制药旨在治疗感染性呼吸系统疾病或全身性疾病,可降低治疗剂量和成本。在优化的蛋白质/稳定剂组合存在下的干燥方法可产生具有更高稳定性的蛋白质固体制剂。根据蛋白质给药途径选择合适的干燥方法并优化工艺参数。随着解决生物制药生产缺陷、开发替代传统干燥方法的新方法以及研究具有更高效稳定作用的新型赋形剂的持续趋势,这些产品未来有望在制药行业占据主导地位。

**关键词:** 稳定性;生物制药;表征;固体制剂;干燥

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## 引言

近几十年来,生物制药(包括肽、蛋白质、疫苗、基因、激素和酶)的生产经历了快速增长(Chen et al. 2021a, b)。在过去16年中,生物制药占FDA批准产品的35%(Vass et al. 2019),预计到2025年,该市场将达到3950亿美元(Guo et al. 2020)。因此,克服这些生物制药的制剂挑战具有重要意义。治疗性蛋白质的大分子量和复杂结构及其对环境应力的敏感性导致多种理化降解,如脱酰胺、氧化、水解、消旋化、异构化、β-消除、二硫键交换、聚集、沉淀和变性(Filipe et al. 2013)。鉴于这些制剂的口服生物利用度低且跨上皮转运有限,胃肠外给药是一个引人关注的方向(Anselmo et al. 2019)。最常见的给药途径是胃肠外给药,通常使用液体制剂进行递送(Zhang et al. 2021a, b);然而,固体制剂可获得更稳定的产品(图1)(Chen et al. 2021a, b)。因此,为保持产品的理化完整性和内在活性(Vass et al. 2019; Mutukuri et al. 2021),必须开发固态制剂方法(Mutukuri et al. 2021)。

**图1** 示意图比较了通过不同给药途径递送生物制药的情况,并显示肺部和/或鼻腔递送如何优于胃肠外给药(Kunde et al. 2022)

液态下,生物分子的不稳定性可导致药物在储存、运输和给药期间发生永久性或可逆性变化(Vass et al. 2019; O'Sullivan et al. 2022a, b)。已采用多种方法来稳定生物制药,如糖基化(O'Sullivan et al. 2022a, b)、脂质化(Egli et al. 2021)以及加入新成分。然而,许多应用的稳定化技术成本高昂,并对某些生物分子的结构和特异性产生不良影响。为提高稳定性,可采用干燥技术(O'Sullivan et al. 2022a, b),如冷冻干燥(FD)、喷雾干燥(SD)、喷雾冷冻干燥(SFD)、超临界流体干燥(SCFD)和临界流体SD,以消除水分并以粉末形式提供更稳定的产品(Vass et al. 2019),具有更长的保质期(Keil et al. 2019)。干燥方法使最终产品的处理更加方便,并最大限度地降低了在运输和储存期间提供冷链(2至8°C)或有时冷冻(-20至-80°C)的费用(O'Sullivan et al. 2022a, b)。在我们之前的研究中,我们报道了可用于稳定生物制药的不同干燥技术和稳定赋形剂(Emami et al. 2018a, b)。在本综述中,我们讨论了用于生产生物制药干粉制剂的最新干燥技术以及治疗性蛋白质的表征测试。与此同时,我们还综述了干粉吸入器主要集中于治疗呼吸系统疾病的局部药物递送。除了通过吸入局部药物递送获益的肺病患者外,糖尿病、骨质疏松症和激素缺乏症患者(Keyhan shokouh et al. 2021)也可享受这种给药方式的简便性和无创性(Emami et al. 2018a, b; Emami et al. 2019; Dhahir et al. 2021)。

## 干燥技术

从各种方法中选择合适的干燥技术取决于给定生物分子的固有特性、期望的给药途径以及干燥程序的费用(Vass et al. 2019)(图2)。

**图2** 影响干燥蛋白质特性的参数总结

### 冷冻干燥(FD)

FD,即冻干法,是最常用的脱水技术,包括三个主要步骤:(1)冷冻,(2)一次干燥和(3)二次干燥。FD过程中的变量,从冷冻阶段降温速率到升华阶段升温至特定温度,再到降温速率和温度循环频率,均可影响最终产品特性,如结晶度、晶体尺寸、孔径甚至结构稳定性(O'Sullivan et al. 2022a, b)。尽管存在高能耗和耗时(从数天到数周完成)(Vass et al. 2019)、冷冻和解冻阶段诱导的应力以及缺乏对所得颗粒尺寸的控制(O'Sullivan et al. 2022a, b)等缺点,FD仍被广泛应用于生产当今市场上超过一半的生物制药(Vass et al. 2019)。冻干产品包括用于吸入或注射目的的单克隆抗体(mAbs)(Hickey et al. 2022)、用于靶向递送系统的高浓度蛋白质产品(Butreddy et al. 2021)、疫苗[DNA(Chen et al. 2021a, b)、mRNA(Cohen 2022)、siRNA和mRNA(Zhao et al. 2020)基础治疗药物(Rehman et al. 2021; Tang et al. 2021)]以及室温稳定的mAb溶液(Zhang et al. 2021a, b)。传统的低玻璃化转变温度(Tg)和低坍塌温度(Tc)赋形剂(如蔗糖)可导致漫长且昂贵的冻干循环,可用新赋形剂(如右旋糖酐)替代(Haeuser et al. 2020)。

薄膜冷冻干燥(TFFD)是一种低温技术,采用介于SFD(10² K/s)和冻干(1 K/s)之间的中等冷冻速率(10²至10³ K/s)(Engstrom et al. 2008),以将液态工程化气溶胶干燥粉末用于肺部药物递送(Hufnagel et al. 2022)。在相对较高的冷冻速率下(如TFFD),可避免溶解溶质颗粒的聚集和任何形式的沉淀分散。此外,这种高产率技术可产生均匀的粒径分布,并且由纳米聚集体微粒组成的低密度脆性基质有利于呼吸递送系统(Sahakijpijarn et al. 2020)。TFFD已被应用于小分子、蛋白质和疫苗的干粉制剂(Wang et al. 2021)。Hufnagel等人应用TFFD将mAb、免疫球蛋白G(IgG)和抗程序性细胞死亡蛋白1(抗PD-1)制成干燥粉末,并研究其气溶胶性能。研究考察了两种应用赋形剂组(海藻糖/亮氨酸75:25 w/w和乳糖/亮氨酸60:40 w/w)的最佳比例以及水或磷酸盐缓冲盐水(PBS)作为TFFD溶剂的效果。研究中mAb载药量分别为0.5%和1% IgG,其中1% IgG与乳糖/亮氨酸(60:40 w/w)在PBS中显示出最佳气溶胶性能;在溶剂方面,PBS比水提高了重现性和气溶胶性能。而含有1% IgG的海藻糖/亮氨酸(75:25 w/w)制剂与载药量一半的mAb相比,细颗粒分数(FPF)显著降低。以相同的乳糖/亮氨酸最佳比例(60:40 w/w)制备1%抗PD-1 mAb,产生的干粉制剂的气溶胶化能力几乎与IgG1-LL-PBS相当[抗PD-1的回收FPF为91.38±1.89,IgG的回收FPF为92.64±1.311]。此外,抗肿瘤坏死因子α(抗TNF-α)mAb以1% w/w(海藻糖/亮氨酸75:25)配制,有趣的是其回收率报告为完全回收,单体含量未发生变化,而在抗PD-1 mAb制剂中,FPF在TFFD过程后从96%下降至79.2%(Hufnagel et al. 2022)。

FD中耗时的干燥步骤——一次干燥,对于含有蔗糖作为冻干保护剂和冷冻保护剂成分的制剂是不可避免的。Haeuser等人研究了如何提高mAb在高温储存下的稳定性。他们使用了不同分子量的多糖右旋糖酐(1、10、40、150和500 kDa)单独以及与蔗糖以不同比例组合。在较高分子量(40-500 kDa)的右旋糖酐和右旋糖酐与蔗糖的重量比下,观察到Tc比蔗糖高20°C。这导致更长的复溶时间和更高的粘度。此外,随着右旋糖酐重量分数的增加,蛋糕开裂程度更高,如果使用更高重量的右旋糖酐则更为明显。添加右旋糖酐还导致更高的Tg值,同时残留水分水平下降。对含有纯右旋糖酐或右旋糖酐/蔗糖1:1混合物的mAb1和mAb2制剂进行了为期两周的40°C蛋白质稳定性分析,考察可溶性聚集体形成。结果显示,FD后,100%右旋糖酐制剂的高分子量物质(HMWs)略有增加1-3%,在40°C储存条件下,所有制剂均显示出显著量的HMWs。就纯右旋糖酐制剂中的HMWs%而言,较高分子量的右旋糖酐显示出较低的HMWs%,尽管与含有较低分子量右旋糖酐的制剂中的HMWs相比,其尺寸更大。mAb1(IgG1,pI~9.4,148 kDa)和mAb2(IgG1,pI~8.2,149 kDa)以1:1右旋糖酐/蔗糖混合物配制。其蛋白质稳定性分析显示FD后HMWs%无变化,但在40°C储存下,含有10-500 kDa右旋糖酐的制剂的HMWs%比纯右旋糖酐制剂低五倍。右旋糖酐的游离末端葡萄糖是糖基化反应的原因,添加蔗糖显著降低了较高百分比的HMWs(Haeuser et al. 2020)。

高浓度治疗性蛋白质的浓度为50至150 mg/mL。这些蛋白质包括血浆来源的免疫球蛋白,典型浓度为50-100 mg/mL的静脉注射免疫球蛋白。Duraliu等人评估了冻干血浆来源IgG在加速和实时储存条件下6至12个月期间的稳定性。(-20°C~<5%相对湿度(RH);20°C,~40% RH;45°C~10% RH)。制备了10至200 mg/mL的一系列IgG浓度,与蔗糖组合时其浓度固定为10 mg/mL,而蔗糖/IgG摩尔比如下变化:1% IgG为439:1;5% IgG为88:1;10% IgG为44:1;20% IgG为22:1。在-20°C、20°C和45°C温度下储存12个月结束时,所有IgG浓度均显示出较高的水分含量百分比,尤其是在较高温度(20°C和45°C)下。10 mg/mL IgG在升高温度下的水分含量约为3-4%,而增加IgG浓度导致水分减少至1-2% w/w。在20°C和45°C下,所有IgG浓度均经历单体损失,其中较高浓度显示出更大的单体损失。考虑到通过ELISA测量的结合活性以及应用抗白喉和抗破伤风IgG作为IgG标志物,在50和100 mg/mL浓度下,在高温和12个月储存后观察到单体含量降低但结合活性适当。同时,在相同条件下单体含量降低。较高IgG浓度(200 mg/mL)由于缺乏完全复溶和超过两小时的溶解时间而显示出可变的ELISA结果(Duralliu et al. 2020)。

### 喷雾干燥(SD)

尽管FD工艺在生产干粉方面具有多项优势,但FD存在一些局限性。FD的限制包括消耗大量时间、能源和资源。此外,FD难以处理大量物料,这在制药工业中至关重要。而且,控制FD中颗粒和蛋糕的特性具有挑战性。这些挑战促使人们寻找替代干燥技术SD(Pinto et al. 2021)。通过SD技术生产干燥粉末涉及将蛋白质溶液雾化到干燥室中一次性干燥并形成固体颗粒,所有步骤在一个步骤中完成。关于功能性赋形剂,两种技术共享相同的稳定剂(Massant et al. 2020)。然而,SD的"连续加工"使其成为制药工业中制造大量稳定干燥粉末的杰出技术(Pinto et al. 2021)。在SD过程中,温度和雾化气体流速是决定颗粒特性的基本参数,如颗粒尺寸、形态和残留水分含量(Wu et al. 2019)。许多喷雾干燥产品已获得批准或上市。自2006年吸入式喷雾干燥胰岛素Exubera®(辉瑞)上市以来,已进行了许多研究以生产喷雾干燥的生物制药(内分泌激素、噬菌体病毒、治疗性酶等)用于治疗疾病(Pinto et al. 2021)。

考虑到赋形剂及其比例对干燥粉末储存稳定性和复溶时间的影响,Massant等人使用两种IgG4 mAb(mAb1和mAb2)作为模型蛋白质,糖类(海藻糖、蔗糖)和一系列氨基酸,包括甘氨酸(Gly)、丙氨酸(Ala)、脯氨酸(Pro)、丝氨酸(Ser)、缬氨酸(Val)、亮氨酸(Leu)、异亮氨酸(Ile)、谷氨酰胺(Gln)、组氨酸(His)、赖氨酸(Lys)、精氨酸(Arg)、苯丙氨酸(Phe)、色氨酸(Trp),作为其制剂稳定剂。根据初步结果,小分子中性和碱性氨基酸与糖基基础(蔗糖、海藻糖)组合显示出缩短的复溶时间和改善的稳定性。在他们研究的第二部分,基于实验设计(DOE)的试验包含16种制剂,其中采用两组必需氨基酸(Lys和Arg)和中性氨基酸(Gly和Pro)的最佳海藻糖/氨基酸比例进行试验。在此试验中,海藻糖浓度从30 mM到120 mM,氨基酸浓度范围为50至150 mM。储存条件设定为25°C和40°C持续13周。除含有高Lys或Gly含量和低海藻糖含量的制剂外,所有制剂均保持无定形状态。Arg在所测试的氨基酸中显著缩短复溶时间并提高储存稳定性。而在其他含氨基酸的制剂中,海藻糖浓度和糖组分在改善稳定性和复溶时间方面发挥关键作用。事实上,Arg的稳定效果非常强,无需添加糖稳定剂来增强稳定性。此外,mAb与稳定剂的重量比应至少为1:1(w/w)才能获得满意的稳定性和复溶时间。在他们的研究中,利用HMWs、相对湿度(RH)和浊度结果评估稳定剂对聚集和储存稳定性的功效(Massant et al. 2020)。

Wu等人评估了两种显著应力(热应力和剪切应力)对增强型绿色荧光蛋白特异性小干扰RNA(EGFP-siRNAs)溶液SD过程中化学完整性、生物活性、产率和颗粒尺寸的影响。因此,就siRNA含量而言,所有喷雾干燥粉末显示出77%至93%的包封率范围,表明过程中有一定程度的siRNA损失,尽管随着入口温度升高,包封率降低。通过测量生产产率观察到产率与雾化气体流速之间的相关性。然而,入口空气温度对产率的影响是可变的,取决于流速。不幸的是,喷雾干燥siRNA的化学完整性可能受到SD过程中颗粒暴露的热应力和剪切应力的严重影响。根据将siRNA溶液暴露于接近出口温度92°C的温度所获得的结果,当加热时间从10分钟变为120分钟时,分解siRNA的百分比增加了52.9%,达到66%。尽管当前SD过程中的出口温度高达92°C和125°C,但siRNA的短时间暴露和溶剂的快速蒸发导致分解低至20%。根据转染效率测试,所有喷雾干燥siRNA的生物活性均低于非喷雾干燥制剂。此外,进一步实验未揭示转染效率与化学完整性之间的任何相关性。换句话说,小程度的化学完整性不会损害喷雾干燥siRNA的生物活性(Wu et al. 2019)。

### 喷雾冷冻干燥(SFD)

SFD是一种引人注目的干燥技术,包括将进料溶液雾化到低温液体(如O₂、N₂或Ar容器)中并干燥冷冻液滴。由于一些独特特性,包括均匀的粒径分布、多孔结构和改善的货架稳定性,形成的颗粒适用于肺部药物递送。该方法已被证明可提高生物药剂学分类系统(BCS)II类药物的溶解度(Adali et al. 2020),生产除前一组药物外的其他药物的可吸入干粉(Liao et al. 2020; Faghihi et al. 2021),并显著提高溶出度(Hu et al. 2019)。尽管SFD非常有利于干燥热敏性材料(Adali et al. 2020),但会对mAb和其他生物制药产生诱导应力,如脱水、冷变性和冰结晶。因此,应用适当的赋形剂来保持其稳定性变得至关重要。

治疗性蛋白质(包括抗体和抗体-药物偶联物)通过1986年FDA批准的首个抗体-药物(muromonab-CD3(Orthoclone OKT3,Janssen-Cilag))进入市场。此后,许多基于抗体的药物已获得批准并商业化(Kim et al. 2016a, b; Singh et al. 2018)。鉴于这些药物在制造过程和储存期间的稳定性至关重要,并且每种单一mAb需要其最佳生产工艺参数,例如赋形剂的类型、组合和浓度(Emami et al. 2018a, b; Emami et al. 2019)(图1)。

Emami等人使用不同氨基酸(包括Leu、Phe、Arg、Gly和半胱氨酸(Cys))在海藻糖存在下构建喷雾冷冻干燥IgG微粒,以研究氨基酸通过SFD方法对IgG稳定性的影响。纯喷雾冷冻干燥IgG导致形成14%的IgG聚集体;然而,使用Leu、Phe或Gly与海藻糖稳定的IgG制剂显示出聚集体<2.2%。Phe与海藻糖的组合在SFD过程中对稳定IgG抵抗不同种类的应力最为有效。Arg和Cys是去稳定剂,分别代表IgG的聚集和片段化。用Leu、Phe或Gly与海藻糖制备的IgG制剂显示出良好的稳定性(40°C和75%相对湿度两个月)。因此,海藻糖与非极性不带电氨基酸的组合对喷雾冷冻干燥IgG制剂显示出最稳定的效果(Emami et al. 2018a, b)。

在Milani及其同事的另一项研究中,将羟丙基β-环糊精(HPβCD)以其替代水、玻璃化和表面活性剂样效应而闻名,与海藻糖一起以不同比例添加到IgG制剂中,比例范围从IgG:HPβCD的上下限1:2和1:0.05。在不同比例的组合中,两种比例为1:2:0.25(IgG:海藻糖:HPβCD)和1:2:0.05的制剂在45°C和60%相对湿度下储存一个月后具有最低的聚集常数(分别为0.46±0.02和0.58±0.01)。测量SFD后和SFD后1和2个月的可溶性聚集体诱导显示出有趣的结果如下:所有制剂的聚集范围为0.01%至0.1%,1:2:2比例达到极小量(0.01%),0.25±0.05%和0.28±0.02%的聚集被报告为1:2:0.25和1:2:0.05在SFD后2个月储存中的最低水平。追踪储存后所有样品的化学降解未显示IgG分子的可见片段。IgG分子主要二级结构β-折叠结构的百分比在SFD后在65.13%至77.82%之间。储存条件下的β-折叠含量略高(66.32-78.15%)。最后,测量FPF和ED作为制剂气溶胶性能的代表。对于所选制剂,1:2:0.25和1:2:0.05比例的FPF值分别为56.43%和48.12%,其各自的ED值分别为93.15%和91.23%(Milani et al. 2020)。

### 超临界流体干燥(SCFD)

在迄今为止讨论的各种现有干燥方法中,SCFD技术因其独特特性而引人关注,包括无毒、不易燃、惰性、可回收和易于通过减压去除(Costa et al. 2021),以及环保(Xu et al. 2018),并使用超临界二氧化碳(scCO₂)作为良性溶剂在如此苛刻的条件下(温度:31.1°C,压力:73.8 bar)加工聚合物。该技术在生产具有最少残留有机溶剂的基于聚合物的多孔微粒方面的可行性值得注意(Xu et al. 2018)。产品中残留的溶剂可能损害储存稳定性和药物给药(Park et al. 2019)。此外,颗粒形态可通过该过程控制,还可实现均匀的粒径(Kankala et al. 2018)。

基于scCO₂的应用,有多种干燥技术可用,如超临界溶剂快速膨胀(RESS)、气体饱和溶液颗粒(PGSS)、二氧化碳辅助气泡干燥器雾化(CAN-BD)、超临界辅助雾化(SAA)/超临界CO₂辅助喷雾干燥(SASD)、膨胀液体有机溶液减压(DELOS)以及超临界CO₂作为抗溶剂。关于生物制品,气体抗溶剂方法是基于超临界干燥的其他方法中最受欢迎的(Wilson et al. 2018)。

在一项研究中,Wu等人采用scCO₂作为喷雾介质和乙醇作为溶剂,通过超临界辅助雾化(SAA)工艺制备HPβCD颗粒。他们旨在研究乙醇作为溶剂对可吸入颗粒形态和尺寸的影响,并优化SAA中涉及的生产这些颗粒的参数。此外,他们的制剂完全通过添加适量Leu设计,已知Leu对干粉气溶胶性能有积极影响。在他们的研究中,考察了几个参数,包括溶剂和HPβCD溶液的浓度(W/W)、沉淀器和饱和器温度以及CO₂/HPβCD的流速比。除了为确定所有变化参数中最实用值而进行的18次测试外,还进行了六次测试以确定不同浓度Leu的影响。测量颗粒尺寸显示,乙醇浓度增加导致更多雾化和颗粒尺寸减小。值得注意的是,向水和CO₂的二元混合物中添加乙醇使CO₂溶解度增加了九倍。尽管乙醇浓度增加对微粉化有积极影响,但其对形状的不良影响也很明显。为避免不规则或壳状颗粒并受益于微粉化,选择54.2%(w/w%)的乙醇浓度。其他最佳参数报告为沉淀器(T_P)和饱和器(T_s)温度分别为373.2 K和353.2 K。在设定的SAA工艺最佳参数T_P:373.2 K、T_s:353.2 K、CO₂/HPβCD流速比:1.8以及HPβCD溶液固定浓度10 mg/mL下,添加Leu以研究制剂的气溶胶性能。13%的质量浓度达到27.8±0.4的FPF值。而将Leu浓度增加至16.7%导致聚集和FPF值降低(Wu et al. 2021)。

在Xu等人进行的另一项研究中,报道了制备纳米嵌入多孔微粒(NEPMs)以递送多药耐药蛋白1(MRP1)siRNA和阿霉素(DOX),以克服肺癌(如小细胞肺癌)中观察到的多药耐药性(MDR)。通过使用超临界抗溶剂工艺(SAS)和CO₂作为工艺中的抗溶剂,他们可以将DOX和预制备的siRNA-壳聚糖(siRNA-CS)纳米颗粒封装到基于聚合物的聚-L-丙交酯(PLLA)中,形成(siRNA-CS-DOX-PLLA PMs),被视为NEPMs。siRNA-CS纳米颗粒的物理特性表征显示球形结构具有窄粒径分布,平均直径为100 nm,载药效率为77.4%,非常显著。这些颗粒可在24小时内持续释放约60%的siRNA。最终微结构表面粗糙,表明纳米颗粒附着良好,高度多孔,平均几何粒径为16.86 µm。考虑到NEPM的报导空气动力学特性,增加DOX含量对D_g或D_a测量值无显著影响,但所有特征均处于肺部递送的最佳水平(10 µm < D_g,1 < D_a < 5 µm,FPF > 50%)。在驱动后0.12 s内实现了NEPM气溶胶化行为的视觉观察,这被认为是良好的移动性。从NEPM中释放60%至80%的包封DOX耗时长达60小时。NEPM在H69AR癌细胞中的亚细胞定位被研究作为其递送效率的指标。根据结果,siRNA-CS纳米颗粒的细胞摄取很高,这些纳米颗粒介导的siRNA释放通过从细胞质逃逸实现。进行抗癌功效测试显示,NEPM有能力将细胞活力降低至约46%,而其他制剂(DOX、DOX-PLLA PMs和NC NEPMs)的结果>80%(Xu et al. 2018)。

### 有前景的干燥技术

到目前为止,已经讨论了几种生产生物制药干粉的方法,但还有其他潜在技术值得一提。非润湿模板粒子复制(PRINT®)技术是一种基于光刻的方法,具有通过调整模具尺寸精确控制颗粒尺寸和形状及其单分散性的潜力(El-Hammadi et al. 2022; Shah et al. 2022)。应用PRINT技术使得从疏水性到亲水性药物的广泛药物负载成为可能。生产的聚乳酸-羟基乙酸共聚物(PLGA)纳米颗粒可以是针状或圆柱形的(El-Hammadi et al. 2022)。该方法已被应用于将蛋白质微模制成高性能干粉(Wilson et al. 2018),合成脂质-聚合物混合纳米载体(Shah et al. 2022)用于递送流感疫苗抗原(Rana 2021)。

另一种广泛传播的方法是流化床干燥,其中含有药物的溶液在具有热气体的流化床系统中喷洒到惰性载体珠上。该方法通常是配制肽口服药物递送系统的首选(Vass et al. 2019),尽管其产品涵盖药物和食品粉末到洗涤剂和肥料(Orth et al. 2022)。因此,Tyagi等人构建了多单元颗粒系统,目的是靶向口服递送胰高血糖素样肽-1(GLP-1)激动剂肽。他们使用流化床系统进行药物层积、密封包衣、缓释包衣、黏附性和肠溶包衣(Tyagi et al. 2021)。

其他方法,即真空干燥、微波干燥和静电纺丝,正引起关注,因为它们显示出比传统干燥方法更高效的潜力(Sharma et al. 2021)。

## 临床试验中的生物制药

生物制药产品市场由单克隆抗体、纯化蛋白质、疫苗、细胞和基因治疗、合成免疫调节剂和重组生物分子(即生长因子、蛋白质、激素以及酶)组成。这一多元化市场在2027年有望实现5341.9亿美元的收入,2022年至2027年的复合增长率为7.32%(Intelligence 2022)。制造这些产品的兴趣日益增加,源于其在治疗许多疾病(包括慢性病毒性肝炎、类风湿性关节炎、银屑病和某些类型癌症)方面更高的疗效。由于这些分子重量大且生物学不稳定,通常的给药途径是胃肠外给药,大多以冻干粉、稀释或浓缩溶液和混悬液形式(Bjelošević et al. 2020)。

另一方面,有可吸入的生物分子蛋白质干粉或溶液,这些产品已经或曾经上市,如Pulmozyme®、Technosphere™ Afrezza®和Exubera®。此外,许多此类产品一直在进行临床试验(Karimi et al. 2022)。表1显示了自2018年以来FDA批准的生物制药产品和临床试验中的生物制药。然而,Resusix®临床试验已终止(Entegrion 2020)。

**表1** FDA批准和临床试验中生物制药的列表

| 生物制品 | 品牌/剂型 | 病症或疾病 | 临床试验编号/STN | 生产方法 | 赋形剂 | 给药途径 | |---------|----------|-----------|----------------|---------|-------|---------|