3.1. Size-Based Approaches
Plenty of protocols exist for EV isolation, including several combined methods [
16,
17]. The gold standard for EV separation is differential ultracentrifugation (dUC, or UC) that combines serial centrifugation steps (
Figure 2A). A standard protocol comprises centrifugation at low speed (300 × g) to remove cells; at medium speed (2000 × g) to remove larger cell debris; centrifugation at high speed (10000 × g) or filtration through a 0.22 μm filter to remove large non-exosomal EVs; and two long, high-speed centrifugation (100 000 × g; 60–70 min) steps to pellet and wash EVs [
18]. dUC allows high concentration of EVs, but its application for industrial-scale EV manufacturing is complicated [
19]. Currently, dUC is the best-characterized method that is used in roughly half the studies related to EVs [
20]. However, separation of EVs with dUC has many disadvantages, including vesicle aggregation [
21], disruption [
22] and loss [
23], contamination with free proteins and their aggregates [
24], and low isolation yield (~25–30%) [
25]. Moreover, dUC is time-consuming and has high equipment requirements. EV pelleting efficiency is dependent on parameters such as sample viscosity and centrifuge acceleration, rotor type and characteristics [
19]. Intra- and interlaboratory variability, as well as poor scalability, make following GMP principles difficult with this method [
26].
Density gradient ultracentrifugation (DGU) is a variation of dUC that uses a medium (usually a solution of sucrose or iodixanol [
27]) of gradated density (
Figure 2B). During the centrifugation process, EVs migrate to their equilibrium fractions according to their size, shape, and density. DGU offers the highest EV purity with almost no protein contamination [
28], as well as reduces vesicle damage and aggregation [
11], but the method is tedious, expensive, low yield, and requires post-purification from gradient media, thus often resulting in considerable EV loss [
19].
During ultrafiltration (UF), a sample is passed through a semi-permeable membrane, so small contaminants (below membrane pore size cut-off) are removed into the filtrate whereas the desired particles are collected in the retentate (
Figure 3A). To remove proteins and small molecules, cut-offs of ~300–750 kDa (~30–75 nm) are a common choice, whereas filters with a higher molecular weight cut-off (i.e., 1000 kDa) can be useful to remove some smaller EVs [
29]. UF is preferred by many researchers as it is fast, simple, and does not require expensive equipment [
30]. UF is considered time-saving and cost-effective, it allows for concentrating EVs, offering a greater isolation yield than dUC [
31]. Also, UF method is established in the industry for protein production and is therefore easily scalable [
32]. However, larger particles that cannot migrate through the membrane can accumulate on the filter upstream surface and block filtration of smaller molecules, resulting in a “cake” formation effect that decreases sample purity [
11,
33]. Other disadvantages of UF are possible EV deformation [
19], non-specific adsorption of EVs on the filter surface, and filter pore clogging [
34].
To reduce the “cake” formation effect, asymmetric depth filtration (ADF) has been proposed for EV isolation [
35]. Depth filters use a porous filtration medium with larger diameter pores to retain particles throughout the medium rather than on the filter’s surface. The filter pores have a tortuous geometry, which allows them to capture larger particles (
Figure 3B). Thanks to this setting, soluble components and small molecules are eluted first, while larger components elute later or get trapped within the filter. DF is a simple, fast, and inexpensive method that provides less filter clogging since the entire filter medium participates in fractionation rather than just its surface.
Tangential flow filtration (TFF), also known as cross-flow filtration, is a more sophisticated version of UF that is based on the same principle. However, in the TFF system, the stream flows tangentially across the UF membrane and a second flow is directed through the membrane (
Figure 3C). Smaller particles are filtered through the membrane, and larger particles are flushed from the filter by tangential flow. TFF is a cyclic process, and filtration can be repeated several times to increase sample purity or perform buffer exchange. TFF is time-saving, reduces material deposition, provides high EV yields, and allows for vesicle concentration [
36,
37,
38]. TFF can be used to isolate EVs from large volumes (thousands of liters) and is established as a scalable industrial approach [
37]. However, TFF can result in vesicle contamination with large proteins and DNA [
15,
39], and therefore often requires a second process (e.g., size exclusion chromatography) to obtain optimal EV purity [
38].
Size exclusion chromatography (SEC) is another prominent method that separates particles by size as they pass through a column filled with porous beads [
40]. Components larger than the pore size are unable to enter the pores of the column and thus elute first, while smaller molecules or particles become trapped inside beads and elute later. This method efficiently eliminates smaller molecules, proteins, and small particles in combination with mild processing conditions that preserve vesicle structure [
41]. SEC provides high purity of isolated EVs, but it is a laborious process that may require specialized equipment [
42,
43]. Although SEC may be used for scaled preparations, it requires a pre-concentration step for processing of large amounts of EV-enriched media [
44] and has relatively low yield [
45].
3.3. Affinity-Based Approaches
EVs can be isolated via immunoaffinity methods based on EV-specific membrane protein molecules, such as CD9, CD63, and CD81. [
49]. In immunoaffinity-based isolation, antibodies are usually attached to magnetic beads to form antibody-conjugated magnetic beads that can pull EV populations from crude material (
Figure 4B) [
15]. Immunoaffinity methods offer high purity [
50] and reduce contamination with soluble proteins [
33]. However, EV markers are not present on every EV subtype [
51]; for instance, only a small number of EVs are positive for both CD63 and CD81 [
52]. Moreover, the interaction between the antibody and the EV marker is not easily disrupted. Harsh elution conditions may destroy EV structure [
53].
Recently, a protocol named EV-Elute has been proposed, which allows recovery of over 70% of bound EVs from antibody-conjugated magnetic beads without compromising EV integrity [
54]. This is achieved by optimizing components of the elution buffer and conditions used for the elution process. Other disadvantages of immunoaffinity methods include high antibody costs, relatively low EV yield [
33], and method difficulties for isolation from large quantities [
55]. On the other hand, aptamers can be used instead of antibodies to lower the cost [
56]; aptamer-marker interactions are also easily reversible in mild conditions that allow to particle isolation that preserves their integrity.
3.4. Chromatography Approaches
To obtain high-purity EVs, multimodal flowthrough chromatography (MFC; also known as bind-elute chromatography) has been introduced [
57]. MFC combines size-exclusion and bind-elute chromatography. MFC resins have an inert shell permeated with size-selective pores that surround an absorptive core. When small molecules and proteins enter the pores, they bind to the absorptive core via hydrophobic and charge interactions. Other molecules larger than the size of the selective pores, including EVs, are excluded from the shell and can be collected in the flowthrough. MFC allows isolating EVs with higher purity (comparable to 2D culture and SEC) even from highly contaminated bioreactor preparations and with negligible sample dilution compared to SEC [
57].
Anion-exchange chromatography (AIEX) is another chromatography-based method that is applied for EV isolation. EVs can be separated by binding to the positively charged column due to negatively charged phospholipids found in EV membranes [
58]. AIEX can be scaled to an industrial level and shows higher sample yield, purity, and size distribution than dUC [
59]. Despite its advantages, AIEX can provide only limited specificity due to co-isolation of different EV subtypes and sample contamination with other negatively charged molecules (nucleic acids, proteins, and other) [
60,
61], in addition to potential damage to the vesicles due to harsh conditions (e.g., acidic buffers) [
41].
A combination of methods is also used to isolate highly purified EVs: indeed, ~60% of current studies combine several methods for EV isolation [
62]. Combined EV isolation assures better purity and specificity than single isolation methods [
32,
63], and the shortcomings of one approach can be addressed by another method. At the moment, the most optimal methods are SEC in combination with either TFF or UF. As aforementioned, both TFF and UF are able to concentrate the samples but yield less pure EV fractions, whereas SEC can result in relatively high EV purity but dilutes the sample. By combining SEC with TFF or UF, highly concentrated EV fractions with even higher purity can be obtained [
64]. Despite the advantages, every additional purification step increases processing time and reduces overall EV yield [
65].
Table 1.
Comparison of different EV isolation approaches.
Table 1.
Comparison of different EV isolation approaches.
Method |
Principle |
Scalability |
Yield |
EV Damage |
Purity |
Equipment requirement |
Cost |
Additional Pre/Post-steps |
Time |
Ref. |
Differential ultracentrifugation (dUC) |
Serial UC steps |
+ |
+ |
↑↑↑ |
++ |
+++ |
+ |
No |
↑↑↑ |
[19,21,22,23,24,25,26] |
Density gradient ultracentrifugation (DGU) |
Separation of EVs by density using gradient medium |
+ |
+ |
↑ |
++++ |
+++ |
++ |
Yes (media removal) |
↑↑↑ |
[11,19,28] |
Ultrafiltration (UF) |
Filtration through semi-permeable membranes |
+++ |
+++ |
↑↑ |
+++ |
++ |
++ |
No |
↑/↑↑ |
[11,19,30,31,32,33,34] |
Asymmetric depth filtration (DF) |
Filtration through porous medium |
++ |
++ |
↑ |
+++ |
++ |
++ |
No |
↑↑ |
[35] |
Tangential flow filtration (TFF) |
Cross-flow filtration through membranes |
++++ |
+++ |
↑ |
+++ |
++ |
++ |
No |
↑↑ |
[11,15,36,37,38,39] |
Precipitation approaches |
EV sedimentation using polymers |
+++ |
++++ |
↑↑/↑↑↑ |
+ |
+ |
++ |
Yes (polymer removal) |
↑↑↑ |
[11,15,46,47,48] |
Affinity-based isolation |
EV capture via specific interactions with EV markers |
+/++ |
++ |
↑/↑↑ |
++++ |
++ |
+++ |
No |
↑↑ |
[33,50,51,52,53,55] |
Size exclusion chromatography (SEC) |
Separation by size through a bead-filled column |
+++ (combined with UF/TFF) |
++ |
↑ |
+++ |
++ |
+ |
Yes (Pre-Concentration) |
↑↑ |
[41,42,43,44,45] |
Multimodal flowthrough chromatography (MFC) |
Combination of size-exclusion and bind-elute chromatography |
+++ (combined with pre-concentration) |
++ |
↑ |
++++ |
++ |
++ |
Yes (Pre-Concentration) |
↑↑ |
[57] |
Anion-exchange chromatography (AIEX) |
Binding of EVs to positively charged column |
+++ |
+++ |
↑↑ |
++ |
++ |
++ |
Yes (Buffer exchange) |
↑↑↑ |
[41,59,60,61] |
3.5. Challenges of EV Preparation
Low EV yield is a major problem for EV research. Poor EV yields occur for two reasons: 1) small amounts of EVs produced by the cells and 2) EV loss during isolation. One liter of conditioned culture media yields approximately 10
9–10
11 EVs using dUC, which is usually enough for only one experiment in one mouse in preclinical studies [
66]. The expected number of EVs needed for therapeutic applications is ~10
13 EVs per dose per patient [
44]. There are many methods to increase EV production by cells, such as mechanical stimulation, serum deprivation, hypoxia, and supplementation with small-molecule drugs and additives [
11], but these approaches can be associated with cell damage and reduced EV quality. At the same time, using dynamic and static 3-dimensional cell cultures can substantially boost EV production in a scalable manner [
67]. However, low yields after isolation are still an issue.
These issues have led researchers to explore alternative EV sources, such as EVs derived from bovine milk or plants. While these sources allow robust production of EVs with high yields, they cannot substitute human EVs for all applications and can cause adverse and unpredictable effects [
64]. Non-human EVs can be immunogenic or allergenic depending on the administration route, dosage, and number/frequency of doses [
68]. Safety of these materials must be validated for each individual case.
There are currently no methods for simultaneously achieving high EV yield and high purity. Highly purifying techniques always lower EV yields [
69]. Sufficient separation from co-purifying components is a challenge because EVs are contaminated with host nucleic acids, and proteins and their aggregates. Carbohydrates (e.g., hyaluronic acid) can be overlooked contaminants as well [
70]. Another possible contaminant is FBS, a common supplement for cell culturing, which is high in endogenous EVs [
71]. However, serum-free conditions can cause stress-induced phenotypic changes in cultured cells, promoting release of EVs containing reactive oxygen species (ROS) and stress-related proteins [
72]. Human platelet lysate is often used as a substitute for FBS, as it is a safe and effective supplement that creates a xeno-free environment suitable for culturing various cell types while reducing the immunologic risks associated with FBS [
73]. On the other hand, the variability of platelet concentrations and the presence of additional bioactive factors in human platelet lysate may affect cell behavior and EV characteristics, compromising the reproducibility and standardization of prepared EVs. Nevertheless, some contaminants can supply EVs with different traits; for example, hyaluronic acid has immunomodulatory properties that may be associated with successful EV applications in cancer therapy and immunotherapy [
74]. Viral contamination must also be monitored, especially for clinical treatment, because viral particles and EVs are of similar size [
15].
Separating specific EV subpopulations from cell culture for further analysis is still a problem. The heterogeneity of EVs poses a challenge to their application as therapeutic carriers in clinical treatments. For instance, in one study, three EV subpopulations with distinct sizes, protein marker content, morphology, and different functional properties were separated using SEC, demonstrating similar results across different cell types [
75].
Additionally, appropriate conditions for storing, handling, and transporting EVs must be determined. One comprehensive study showed that freezing EVs in phosphate-buffered saline (PBS) greatly reduced EV recovery, and proposed PBS supplemented with human serum albumin and trehalose as the optimal EV storage method [
76]. Other recent studies have utilized EV lyophilization to facilitate handling and transportation and to prolong the shelf-life of the final product [
77,
78]. However, further exploration of effects of lyophilization on the integrity of EV membranes is necessary [
79]. Finally, different storage conditions may be optimal for EVs from different cell sources or for EV subpopulations [
80].
Scalable manufacturing and batch-to-batch variability of EVs are other crucial issues facing clinical therapy. To address these, isolation methods suitable for large-scale applications, such as TFF, SEC, or MFC, can be applied. Bioreactors can be used to produce therapeutically relevant concentrations of EVs while maintaining consistent particle size and phenotype [
81,
82].
Another problem is the biomolecular (protein) corona and effects of different isolation methods on its composition. The surface of most of nanoparticles (NPs) is well known to play a pivotal role in their behavior and functionality. The biomolecular corona can be characterized as spontaneous adsorption of proteins, lipids, sugar moieties, nucleic acids, and metabolites onto NP surfaces [
83] due to their interaction with NP surface molecules in biological fluids. Notably, the corona is formed rapidly (<30 seconds) [
84]. After corona formation, NPs’ physicochemical properties, targeting abilities, and biological responses are dictated by the adsorbed molecules [
83,
85], posing difficulties for predicting how the biomolecular corona may affect NP activity in vivo due to its dynamic nature. Coronas form on the surface of different kinds of NPs, including lipid-based NPs [
86,
87], polymeric NPs [
88], and inorganic NPs [
89]. Recently, biomolecular coronas were shown to be generated around EVs as well [
90]. Additionally, it was demonstrated that the isolation method can deform the biomolecular corona: UC and TFF may change its composition and abrogate EV function [
91].