Currently, UC-MSCs have been extensively utilized in clinical trials [11, 12, 34]. However, there has been limited focus on developing SOPs for GMP to ensure consistent quality of these cells. In this study, we established a standardized method for isolating UC-MSCs, which is outlined as follows: First, Wharton's jelly was extracted and cut into tissue fragments measuring 1–4 cubic millimeters. GMP-grade digestive enzyme (collagenase NB6 GMP) was added at a concentration of 0.4 PZ U/mL, and the digestion process was conducted for a duration of 3 hours. After digestion, the cell suspension was diluted with PBS and filtered using a cell strainer. For Wharton's jelly weighing above 20 g, the cells obtained from digestion could reach a minimum of 2×106 cells to be seeded in a single-layer cell factory. Subsequently, the culture medium was exchanged after 5 days of culture, with subsequent medium exchanges occurring every 3 days until days 10–15. At this stage, P0 cells can be harvested for further production. The parameters within this method were optimized to ensure the generation of high-quality UC-MSCs.
The explant method and enzymatic digestion method are the two main approaches for isolating UC-MSCs [20]. In this work, we conducted a parallel comparison using the same umbilical cord and the same weight of Wharton’s jelly. Our findings revealed that the enzymatic digestion method demonstrated a faster start-up and a shorter culture time during the initial passage (P0). However, after subsequent passages, there were no significant differences between the two methods in terms of cell proliferation, cell viability, and immunophenotype. This suggests that damage caused by enzymatic digestion can be recovered during the culture process. Additionally, the enzymatic digestion method can be easily translated into an automation platform, making it more suitable for GMP-compliant processes in a standardized manufacturing setting [35, 36].
Our findings indicated a positive correlation between the initial cell seeding density and the number of cells collected at P0 within the same sample using the enzymatic digestion method. However, we observed no correlation across different samples due to the individual differences and intricate composition of umbilical cord cells, posing a challenge in determining an appropriate initial cell seeding density. The UC tissue comprises two umbilical arteries, one umbilical vein, and the allantois embedded in Wharton’s jelly and is surrounded by a single layer of amnion. Multiple cell types are present within the UC, including mesenchymal stem cells (MSCs), endothelial cells, epithelial cells, fibroblasts, and cord blood cells. MSCs in Wharton’s jelly are primarily found in the perivascular region nearest to the umbilical vessels, with fewer in the intervascular region and the least in the subamniotic region [37, 38]. Research studies have shown that the colony-forming unit (CFU) derived from primary human umbilical cord perivascular (HUCPV) cells was 1 CFU for every 333 cells [39], while another study reported a CFU-F frequency of 1:1609 in nucleated cells from the umbilical cord [40]. These discoveries further support our research results.
Human platelet lysate (hPL) is widely used as an alternative to fetal bovine serum (FBS) in the ex vivo expansion of MSCs. hPL contains a high concentration of growth factors, adhesion molecules, and chemokines, making it suitable for the production of GMP-compliant cell products [41–44]. Compared to FBS, hPL offers several significant advantages, including enhanced proliferation behavior, reduced population doubling time, preservation of clonogenicity, increased CFU-F size, maintenance of characteristic immunophenotype, preserved in vitro trilineage differentiation capacity, maintained in vitro T-cell immunosuppression, and absence of in vivo tumorigenicity. More importantly, the use of hPL eliminates the risks associated with the transmission of animal-derived viruses [45].
In our study comparing the effects of different concentrations (2%, 5%, and 10%) of hPL on primary cell expansion, interesting outcomes were observed. The results demonstrated that both 2% and 5% concentrations showed similar levels of cell expansion. However, using a 10% concentration resulted in decreased cell expansion. This finding is consistent with previous studies. According to Shansky et al., a 5% concentration of hPL was found to be more effective than both 1% and 10% concentrations in supporting AT-MSC growth. Similarly, Azouna et al. reported that the PDT of 5% hPL was not significantly lower than that of 10% HPL or a combination of 10% FBS and 5% hPL [46, 47]. A meta-analysis has shown that 5% hPL is superior to 10% FBS [48], and Kirsch et al. found that even a lower concentration of 2.5% hPL exhibited a higher proliferation and differentiation rate compared to 10% human serum (HS) or 10% fetal calf serum (FCS) in AT-MSCs [49]. Notably, the discussed above studies conducted their experiments by supplementing basal media, such as α-MEM or DMEM, with additional components. Moreover, it was discovered that when using defined serum-free mesenchymal stem cell media that have been optimized for growth factors, the concentration of hPL can be further reduced to 1% or even as low as 0.5% [50–51]. This observation may provide an explanation for the findings of our study, suggesting that the efficacy of hPL in supporting MSC growth and function can be maximized even at lower concentrations when used in conjunction with serum-free media formulations.
According to a study by Ikebe et al., the use of MSCs in clinical trials from 2007 to 2013 showed that 23% of trials used cells from passage 1 or less, 71% used cells from passages 1–5, and only 6% used cells from passages over 5 [52]. Sareen et al. demonstrated that an increase in passage number (from P3 to P7) in cell culture did not have a significant effect on the immune privilege of MSCs [53]. However, another study found that cells gradually lost their typical fibroblast-like spindle shape from P3 to P8, resulting in elevated morphological abnormalities and inhomogeneity. The cell population doubling rate also decreased [54]. Zhao et al. found that cells at P3, P6, and P15 showed similar morphology, biomarker expression, and cytokine secretion. However, the therapeutic effect on aGVHD in vivo declined at P15 [55]. Yu et al. observed that MSCs grew well for 20 population doublings (PD) but experienced cellular senescence at approximately 40 PD [56]. Based on our stability study, it was found that passages 2 to 5, with a PD of less than approximately 20, were the better passages in terms of high viability and proliferation ability, particularly passage 2 or 3. For allogeneic therapy requiring an abundant number of cells, passages 4 or 5 may be the most suitable.
When transitioning the culture of MSCs from flasks to cell factories, whether at P0 or subsequent passages, the proliferation rate tends to decrease. This can be attributed to the heterogeneity of the physical and chemical environment, as well as the emergence of concentration gradients in cell factories, mainly due to gas exchange occurring at the medium/headspace gas interface [57].
However, despite the decline in the cell proliferation rate, successful scale-up of MSC manufacturing has been achieved in our study, resulting in high-quality drug products. These included high cell viability, maintenance of a stable immunophenotype, low cellular senescence percentage, stable karyotype, and maintenance of multilineage differentiation potential. Furthermore, MSCs showed potent inhibition of lymphocyte proliferation and were free from microbial contamination. The theoretical quantity of cell formulation reached 1013 from one UC.
Cell surface markers are one of the key indicators used to identify MSCs. In addition to testing the marker expression defined by the International Society for Cellular Therapy (ISCT) [4], we also detected the expression of other markers, such as adhesion molecules CD44, CD29, and CD166, functional marker CD146, immunogenic markers HLA-ABC, and costimulatory molecules CD40, CD80, and CD86. Our results revealed that CD73, CD90, CD105, CD44, CD29, and CD166 were expressed at levels higher than 95%, which are currently used to define MSCs [58]. On the other hand, CD45, CD34, CD79a, CD14, and CD31 were expressed at levels lower than 2%, implying a high MSC purity. Furthermore, we found that HLA-DR and costimulatory molecules CD40, CD80, and CD86 were expressed at low levels, while HLA-ABC was expressed positively. HLA-ABC plays a role in protecting MSCs from destruction by natural killer cells, while MHC-II helps in evading immune recognition by T cells. The costimulatory molecules CD40, CD80, and CD86 are part of the second signaling system for T lymphocyte activation. These findings indicate that UC-MSCs manufactured by our method are unlikely to trigger an immune response and can evade host immune attack in vivo [59, 60]. Recent research has shown that CD146 is a potency marker. The CD146+ subpopulation has enhanced immunosuppressive capacity, resulting in improved therapeutic outcomes [61, 62]. We found that the expression of CD146 gradually decreased with increasing passages, indicating that higher passages should be unsuitable for clinical practices. Interestingly, the expression of all the mentioned above markers aligns with the results of Miryam Mebarki et al. [12].
It is worth noting that although our study established GMP-compliant separation methods, manual operations involved in extracting Wharton's jelly and mincing the umbilical cord increase the risk of contamination. Some successful research studies have utilized the entire umbilical cord for digestion without the need to open and remove the vessels to obtain UC-MSCs [63, 64]. However, it is important to mention that these studies were conducted using umbilical cords of approximately 1 cm in length, and the results for longer lengths are still unknown. Therefore, further optimization of the separation method is still required to automate the process and improve consistency. Additionally, our study highlights certain limitations associated with the use of cell factories, suggesting a shift toward the use of bioreactors. Bioreactors allow for precise monitoring and tight regulation of essential culture parameters, including pH value, temperature, dissolved O2, and CO2 levels [57, 65]. This trend of utilizing bioreactors offers promising advantages in terms of enhanced control and scalability for MSC production.