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Article

The Impact of Formulation and Freeze Drying on the Properties and Performance of Freeze-Dried Limosilactobacillus reuteri R2LC

by
Nisha Tyagi
1,2,
Zandra Gidlöf
3,4,
Daniel Tristan Osanlóo
3,4,
Elizabeth S. Collier
3,5,
Sandeep Kadekar
2,
Lovisa Ringstad
2,
Anna Millqvist Fureby
3,4 and
Stefan Roos
1,*
1
Department of Molecular Sciences, Uppsala BioCenter, Swedish University of Agricultural Sciences, 750 07 Uppsala, Sweden
2
Ilya Pharma AB, Dag Hammarskjölds väg 30, 752 37 Uppsala, Sweden
3
RISE Research Institutes of Sweden, 114 28 Stockholm, Sweden
4
Department of Food Technology, Engineering and Nutrition, Lund University, 221 00 Lund, Sweden
5
Department of Health, Medicine and Caring Sciences, Linköping University, 581 83 Linköping, Sweden
*
Author to whom correspondence should be addressed.
Appl. Microbiol. 2023, 3(4), 1370-1387; https://doi.org/10.3390/applmicrobiol3040092
Submission received: 24 October 2023 / Revised: 24 November 2023 / Accepted: 28 November 2023 / Published: 3 December 2023

Abstract

:
Freeze drying is a commonly used method for preserving probiotic bacteria and live biotherapeutic products. Before drying, the bacterial cells are formulated with a lyoprotectant, and the design of these two process steps are crucial to achieve a high-quality product. There are several factors that may affect the biological and physicochemical properties of the freeze-dried cells and we have used a Design of Experiment approach to investigate the effects of formulation and freeze-drying parameters on properties and performance of Limosilactobacillus reuteri R2LC. The biological characteristics of the dried bacteria were evaluated by measuring cell survival, metabolic activity and stability, and physicochemical characteristics were studied using visual inspection, differential scanning calorimetry (DSC), scanning electron microscopy (SEM), and analysis of residual moisture content and bacterial aggregation. A comparison between the lyoprotectants trehalose and sucrose showed that the latter gave better freeze-drying survival, metabolic activity, and storage stability. We also want to highlight that there was a correlation between bacterial concentration, metabolic activity, and aggregation of bacteria, where a higher concentration (1010 CFU/mL) resulted in both higher metabolic activity and aggregation. Several other process and formulation factors affected both the biological and physicochemical properties of freeze-dried L. reuteri R2LC and it could be concluded that care must be taken to develop a production method that generates a product with high and consistent quality. These results may, or may not, be strain specific.

Graphical Abstract

1. Introduction

With the growing interest in microorganisms with health-promoting properties in the pharmaceutical and food industries, robust production methods are in demand. Achieving high viability (number of live bacteria), storage stability, and metabolic activity (vitality) is required for high-quality probiotic and live biotherapeutic products (LBP). Commercially, probiotic strains are distributed either in the form of food/probiotic-based food products (such as yogurt and nutrition bars) or dried and formulated as capsules, such as tablets, chewing gums, oil suspensions, or powders, e.g., packaged in sachets [1].
Freeze drying is a widely used method to stabilize probiotics or LBPs, which removes water from the microorganisms to achieve preservation of their viability, metabolic activity, and improve the storage stability of the products. During the freeze-drying process, the cells are exposed to stressful conditions such as oxidative stress, osmotic stress, dehydration, and damage due to ice crystal formation [2,3]. Therefore, it is important to optimize the process parameters with the aim of alleviating the stress and obtaining potent, reproducible, and stable products. The freeze-drying process consists of three steps: (1) Freezing; (2) Primary drying: removal of frozen water by sublimation; and (3) Secondary drying: removal of residual/unfrozen water by desorption. Several factors affect the properties of freeze-dried bacteria, such as the cultivation method (e.g., substrate, initial cell concentration, and time of harvest) [4,5,6], type and concentration of lyoprotectant [7,8], and the freeze-drying process [9,10]. The lyoprotectant plays an important role in protecting the properties (biological and physicochemical) of freeze-dried products. It is known that many anhydrobiotic plants [11] and animals [12,13] are protected from desiccation by accumulating disaccharides. Therefore, to mimic this strategy, disaccharides such as sucrose [7,14] and trehalose [15,16] are often used as lyoprotectants. These types of lyoprotectants protect the freeze-dried cells by forming an amorphous glassy matrix and high viscosity that prevent the cells from mechanical damage and degradation of proteins [17], and preserve the functionality/bioactivity and stability of the cells after freeze drying [18,19]. The effectiveness of the lyoprotectant is also dependent on the glass transition temperature of the sugars, a temperature at which material transition to a glassy or viscous state [20].
One way to promote the efficiency of freeze drying is to include an annealing step in the process, which involves keeping the product at a temperature above the glass transition temperature for about 15 min, resulting in increased ice crystal growth and ultimately lower water content in the dried product [21]. Previously, it has been shown that annealing with trehalose phosphate as the lyoprotectant is effective in achieving an efficient drying and increased stability of a strain of Lactobacillus acidophilus [22]. As a general goal, low water activity (<0.2) and residual water content (<5%) are required to obtain robust and stable freeze-dried probiotics [23].
The aim of this study was to investigate the influence of formulation and annealing on biological properties and physicochemical characteristics of freeze-dried Limosilactobacillus reuteri R2LC. This is a well-studied strain that has been shown to ameliorate acetic acid or DSS-induced colitis in rats [24] and mice [25]. In a recent paper, R2LC has been shown to mediate its anti-inflammatory effect and modulate the intestinal microbiota by transmitting probiotic signals to immune cells present in Peyer’s patches [26]. The strain also has antimicrobial activity mediated by a polyketide [27]. We used a Design of Experiment (DOE) approach to evaluate the effects of different lyoprotectants (sucrose and trehalose) with concentrations between 10 and 20%, different bacterial concentrations (109 and 1010 CFU/mL), and annealing. The biological properties analysed included viability, metabolic activity, and stability, and the physicochemical characteristics analysed included water content, matrix structure, cake appearance, glass transition temperature, and aggregation of the bacteria.

2. Materials and Methods

2.1. Experimental Design

To investigate the impact of formulation and freeze drying on the biological and physicochemical properties of R2LC, a Design of Experiments (DoE) approach was taken. In this study, four different factors were investigated: type of lyoprotectant (sucrose and trehalose), lyoprotectant concentration (10, 15, and 20%), bacterial concentration (109 and 1010 CFU/mL), and the freeze-drying process (with and without annealing). MODDE version 13 (Sartorius Data Analytics, Umeå, Sweden) was used to generate a full factorial screening study with 24 independent runs (Table S1).

2.2. Cultivation of Limosilactobacillus reuteri R2LC

A glycerol stock (15%) working cell bank was prepared and kept at −80 °C. The main cultivation was performed in 8 L bioreactor (Belach Bioteknik, Stockholm, Sweden) which was inoculated to a starting OD600 of 0.2. Sterilization of the media component (yeast extract and yeast peptone) and bioreactor was conducted at 121 °C for 15 min; and then 5 L of growth medium (0.15 g MnSO4·H2O, 25 g C2H3NaO2, 10 g K2HPO4, 5 mL Tween 80, 0.5 g L-cysteine hydrochloride monohydrate, 0.5 g MgSO4·7H2O, 11.5 g sodium citrate tri-basic monohydrate, glucose (12.5 g/L), 50 g yeast extract (autoclaved) and 50 g yeast peptone (autoclaved)) was filtered sterilized into the bioreactor. The pH and temperature of the bioreactor was set to 5.7 and 37 °C, respectively, and a stirring speed of 200 rpm was used. Cultivation was carried out until the glucose concentration was not detectable (approximately 11–12 h). Glucose concentration was measured using a blood glucose tester (HemoCue AB, Ängelholm, Sweden).

2.3. Formulation/Sample Preparation

The cells were harvested and concentrated in two steps. First, the bacterial cells were concentrated 10× with a 750 kDa hollow fiber filter (GE Healthcare Biosciences Corp, Piscataway, NJ, USA). Secondly, cells were washed and concentrated sevenfold with 50 mM phosphate buffer and concentrated to around 1010 CFU/mL. One part of the concentrate was diluted to 109 CFU/mL in 50 mM phosphate buffer. The two cell suspensions were mixed 1:1 with different lyoprotectants (20–40% solutions of sucrose and trehalose). The final formulations were composed of 1010 or 109 CFU R2LC/mL in 10, 15, or 20% of sucrose or trehalose (in total 12 combinations). The bacterial suspensions were set on hold at 4 °C overnight and stirred at 200 rpm for 10 min before the filling process. The bacterial suspensions were kept under stirring during the filling process. A volume of 1 mL was filled into 2R glass vials (Schott Pharma, Lukacshaza, Hungary), and half stoppered in preparation for lyophilization.

2.4. Freeze-Drying

The formulated cells were freeze dried using a Christ, Epsilon 2-6D LSCplus (Martin Christ Gefriertrocknungsanlagen, Munich, Germany). Samples were divided in two sets: with and without an annealing step. Freezing took place by decreasing the temperature from 20 °C to −45 °C at a rate of 0.36 °C/min and holding it for 3 h. Annealing was introduced by increasing the temperature to −15 °C, hold for 3 h, and then decreased to −45 °C at a rate of 0.36 °C/min and holding it for 2 h. Primary drying was performed by increasing the temperature from −45 °C to −20 °C at a rate of 0.63 °C/min and decreasing the chamber pressure to 0.10 mBar and holding those settings for 45 h. The secondary drying was carried out by decreasing the pressure to 0.01 mBar and increasing the temperature to 20 °C at a rate of 0.17 °C/min and holding it for 25 h [28]. The vial stoppers were closed at 750 mBar. The vials were crimped with an aluminum cap and stored at −80 °C until used.

2.5. Visual Inspection

The cake appearance was evaluated on the basis of a scoring system (1–5). Score (1) signifies an intact and homogenous cake, (2) intact, heterogenous cake structure and dark yellow bottom, (3) shrinkage of the cake around the edges without change in the height, (4) partially collapsed cake (40–60%), and (5) a collapsed cake (>60%) (Table S2) [29].

2.6. Aggregation

The samples with lower (109 CFU/mL) and the highest (1010 CFU/mL) bacterial concentrations were diluted using saline solution (0.9% NaCl) 1:100 and 1:200 times respectively. The diluted samples were analysed using flow cytometry with a Cytoflex S (Beckman Coulter, Indianapolis, IN, USA). The setting parameters were as follows: gain was set to 1000 for side scatter (SSC) and forward scatter (FSC), and the threshold was set to 50,000 for FSC and 10,000 for SSC. For each sample, 105 events were recorded. Similar conditions were used for analysis of a control that consisted of standard diameter of 6 µm polystyrene beads (L34856) that had been diluted 1:10 in saline. The recorded data was then analysed using the FlowJo software version 10 (FlowJo, Ashland, OR, USA). After the selection of log scale, gating was selectively drawn around the 6 µm beads pattern and this gating was used for all samples. Particles above 6 µm were considered as aggregates. The aggregation (%) was calculated as (no. of events counted in the bead region × no. of events in the bacterial region)/100. All measurements were completed in duplicates.

2.7. Water Content

The water content of the freeze-dried bacteria was measured using Karl Fischer Titration (Metrohm Ltd., Herisau, Switzerland) [30]. First, Hydranal-Methanol dry (blank) was measured in triplicates; the value was below 0.3%. The weight of empty and freeze-dried vials was measured, then bacterial cells were resuspended into dry Hydranal-methanol. Again, the weight was measured prior to incubation at room temperature for 1 h (to extract the water from the sample). Each sample was measured in triplicate.

2.8. Scanning Electron Microscopy (SEM)

Samples were collected by cutting out a vertical cross section of the freeze-dried cakes. These cross sections were positioned on circular stubs with double-sided adhesive carbon tape, and then placed in a Quanta 250 FEG ESEM Scanning Electron Microscope (FEI, Brno, Czech Republic). SEM images were collected with a Large Field Detector (LFD), using a 5 kV beam, under 60 Pa pressure. A minimum of two spots in the top and bottom parts of the freeze-dried cake were examined, employing magnifications of 100×, 500×, 1000×, and 2500× [28]. Porosity (%) of the material was evaluated by analysing the scanning electron microscopy images with ImageJ version 1.54e (National Institutes of Health, Bethesda, MD, USA) [31,32].

2.9. Differential Scanning Calorimetry

The glass transition temperature of freeze-dried L. reuteri R2LC-formulations were measured using differential scanning calorimetry (DSC; DSC 1 STARe system, Mettler Toledo, Columbus, OH, USA). The instrument was calibrated prior to the measurements; zinc and indium were used as reference materials. The reference material checks (Tm and ΔH) were within acceptable limits. The freeze-dried cake was cut horizontally and crushed; samples were taken in the range of 1–5 mg. The samples were weighed in aluminium pans, sealed with a lid, and an empty and sealed aluminium pan was used as a reference. To measure the glass transition temperature, samples were first kept at 20 °C and held for 1 min with a rate of 10 °C/min, then heated up to 90 °C at the heating rate of 10 °C/min. Secondly, the samples were again cooled to 20 °C and thereafter heated to 130 °C with a heating rate of 10 °C/min [28]. The measurements were completed under a nitrogen gas flow of 50 mL/min and each sample was analysed in duplicate.

2.10. Cell Viability

Freeze-dried bacteria were rehydrated in 1 mL MRS broth, tenfold serially diluted and plated on MRS (Sigma, Saint Louis, MO, USA) agar plates, which were incubated anaerobically at 37 °C for 48 h. The colonies were counted in an interval of 20–200 colonies per plate and survival % was calculated in terms of before and after freeze drying. The measurements were completed in duplicate.
X v = N 0.1 10 y
where Xv is cell viability, N is the number of colonies counted per plate, y is the tenfold dilution plated, and 0.1 represents 0.1 mL (100 µL) plated.

2.11. Metabolic Activity

L. reuteri R2LC produces lactic acid as a metabolic end product and this acidification was used to evaluate the metabolic activity of freeze-dried cells [33]. The freeze-dried cells were rehydrated with 1 mL of MRS broth and incubated at 37 °C without agitation for 2 h. To analyse the acidification rate, pH was measured at room temperature, at time points 0, 1, and 2 h. The high (1010 CFU/mL) R2LC concentration was diluted 10 times with MRS media before the cultivation.

2.12. Storage Stability

Accelerated storage stability of all freeze-dried variants was investigated by incubation of the vials at 37 °C for 4 weeks. Visual appearance, viability, metabolic activity, and residual water content were analysed at the timepoints 0, 2, and 4 weeks.

2.13. Statistical Analysis

The data were analysed statistically using analysis of variance (ANOVA) with post hoc Tukey HSD multiple comparisons test, Kruskal–Wallis test, and Pearson’s correlation analysis in JASP version 0.17.2.1 (University of Amsterdam, Amsterdam, The Netherlands) [34]. To verify that the data complied with the assumptions of ANOVA, normal Q-Q plots were visually inspected and Shapiro–Wilk tests were performed. All tests were performed with α = 0.05. Raincloud plots were used to visualize the results for individual analysis, probability distribution, and key summary statistics (mean and relevant confidence intervals) [35]. The effect size was described in terms of partial eta squared (η2p), which describes the relative proportion variance explained by each factor included in the analysis.

3. Results

Limosilactobacillus reuteri R2LC was grown in a bioreactor, whereafter it was formulated and lyophilized using a total of 24 different combinations of bacterial concentrations, lyoprotectants, and freeze-drying programs (Figure 1). The formulated and freeze-dried R2LC was subjected to evaluation of both physicochemical and biological outcomes.
Figure 1. Outline of the study including tested variables and characterization of freeze-dried L. reuteri R2LC.
Figure 1. Outline of the study including tested variables and characterization of freeze-dried L. reuteri R2LC.
Applmicrobiol 03 00092 g001

3.1. Effects of Experimental Factors on Physicochemical Properties of Lyophilized R2LC

The effects of varying the selected experimental factors (type and concentration of lyoprotectant, bacterial concentration, and freeze-drying program) on the measured physicochemical outcomes are summarized in Table 1, Table 2, Table 3, Table 4 and Table 5 and Figure 2, Figure 3, Figure 4, Figure 5 and Figure 6. Statistically significant differences, including the associated effect sizes (η2p) are highlighted in the tables and detailed post hoc tests are included in the supplementary data sheets.
Table 1. Main effects and interactions of the experimental factors affecting water content. p-values in bold indicate statistically significant effects.
Table 1. Main effects and interactions of the experimental factors affecting water content. p-values in bold indicate statistically significant effects.
FactorsFpη2p
Lyoprotectant type14.4950.0040.617
Annealing6.0350.0360.401
Lyoprotectant concentration33.819<0.0010.883
Bacterial concentration27.711<0.0010.755
Lyoprotectant × Annealing5.3260.0460.372
Lyoprotectant × Lyoprotectant concentration9.5110.0060.679
All factors significantly affected the water content of freeze-dried R2LC, and in particular using the highest concentration of sucrose (20%) gave an elevated water content (t = 0.271, ptukey = 0.004) (Figure 2 and Table S3). Also, the concentration of bacteria had an impact and 109 CFU/mL resulted in significantly higher water content than 1010 CFU/mL using sucrose (t = 4.933, ptukey = 0.004) as lyoprotectants (Figure 2). Furthermore, annealing resulted in significantly elevated water content in the highest (20%) sucrose concentration (t = 10.829, ptukey = 0.047).
Figure 2. Effect of lyoprotectant concentration (A), bacterial concentration (B) and type of lyoprotectant (sucrose and trehalose) on water content of freeze-dried R2LC. LC: Lyoprotectant concentration; BC: Bacterial concentration, and WC: Water content. Datasets with different letters are significantly different (p < 0.01; data presented in A,B are not compared). (A): violet represents 20%, orange 15% and green 10% lyoprotectant concentration, respectively; (B): orange represents 109 CFU/mL and green 1010 CFU/mL R2LC.
Figure 2. Effect of lyoprotectant concentration (A), bacterial concentration (B) and type of lyoprotectant (sucrose and trehalose) on water content of freeze-dried R2LC. LC: Lyoprotectant concentration; BC: Bacterial concentration, and WC: Water content. Datasets with different letters are significantly different (p < 0.01; data presented in A,B are not compared). (A): violet represents 20%, orange 15% and green 10% lyoprotectant concentration, respectively; (B): orange represents 109 CFU/mL and green 1010 CFU/mL R2LC.
Applmicrobiol 03 00092 g002
ANOVA revealed significant effects of lyoprotectant type and bacterial concentration on glass transition temperature (Tg) (Table 2 and Table S4). The Tg for the samples containing trehalose was around 30–40 °C higher than for samples with sucrose (Figure 3). Post hoc analysis showed that the type of lyoprotectant had a large impact on the glass transition temperature, where trehalose resulted in a significantly higher Tg than sucrose (t = 15.930, ptukey < 0.001) (Figure 3). In addition, the concentration of bacteria had a significant (ptukey = 0.010) effect on the glass transition temperature (Table 2 and Figure 3). Also, a significantly higher Tg was observed at high (1010 CFU/mL) concentration of both sucrose and trehalose (Figure 3B).
Table 2. Main effects and interactions of the experimental factors affecting glass transition temperature (Tg) of freeze-dried R2LC. p-values in bold indicate statistically significant effects.
Table 2. Main effects and interactions of the experimental factors affecting glass transition temperature (Tg) of freeze-dried R2LC. p-values in bold indicate statistically significant effects.
FactorsFpη2p
Lyoprotectant type253.768<0.0010.861
Annealing0.4620.5000.011
Lyoprotectant concentration1.4670.2430.067
Bacterial concentration7.3050.0100.151
Annealing × Bacterial concentration10.2980.0030.201
Lyoprotectant concentration × Bacterial concentration4.4220.0180.177
Note. Type III Sum of Squares.
Figure 3. Effect of high (A) and low (B) bacterial concentration and type of lyoprotectant on glass transition temperature of freeze-dried R2LC. Datasets with different letters are significantly different (p < 0.01; data presented in A,B are compared). Green represents samples with sucrose and orange represents samples with trehalose as lyoprotectant.
Figure 3. Effect of high (A) and low (B) bacterial concentration and type of lyoprotectant on glass transition temperature of freeze-dried R2LC. Datasets with different letters are significantly different (p < 0.01; data presented in A,B are compared). Green represents samples with sucrose and orange represents samples with trehalose as lyoprotectant.
Applmicrobiol 03 00092 g003
The lyoprotectant type, lyoprotectant concentration, and bacterial concentration significantly impacted the aggregation of freeze-dried R2LC (Table 3). Post hoc analysis revealed that the difference between sucrose and trehalose was statistically significant t = −2.329, ptukey = 0.022 (Table S5). Also, the higher concentration of bacteria (1010 CFU/mL) promoted aggregation and gave approximately 2 times more aggregates than for the lower concentration of bacteria, when using formulations with both sucrose (t = 19.757, ptukey < 0.001) and trehalose (t = 15.634, ptukey < 0.001) as a lyoprotectant (Figure 4 and Table S5).
Table 3. Main effects and interactions of the experimental factors affecting aggregation of freeze-dried R2LC. p-values in bold indicate statistically significant effects.
Table 3. Main effects and interactions of the experimental factors affecting aggregation of freeze-dried R2LC. p-values in bold indicate statistically significant effects.
FactorsFPη2p
Lyoprotectant type5.4250.0220.062
Annealing2.2500.1370.027
Lyoprotectant concentration6.4180.0030.135
Bacterial concentration625.580<0.0010.884
Lyoprotectant × Annealing13.163<0.0010.138
Lyoprotectant × Bacterial concentration7.8510.0060.087
Figure 4. Effect of low (A) and high (B) bacterial concentration and type of lyoprotectant (sucrose and trehalose) on aggregation of freeze-dried R2LC. Datasets with different letters are significantly different (p < 0.01; data presented in A,B are compared). Green represents samples with sucrose and orange represents samples with trehalose as lyoprotectant.
Figure 4. Effect of low (A) and high (B) bacterial concentration and type of lyoprotectant (sucrose and trehalose) on aggregation of freeze-dried R2LC. Datasets with different letters are significantly different (p < 0.01; data presented in A,B are compared). Green represents samples with sucrose and orange represents samples with trehalose as lyoprotectant.
Applmicrobiol 03 00092 g004
Scanning electron microscopy was carried out for the characterization of the matrix structure and observation of bacterial structures. The matrices for all samples were amorphous (examples are seen in Figure 5). Bacterial cells were not visible in formulations with the lower bacterial concentration (Figure 5A,B) because they were well-covered by the matrix (Figure 5A), while for the higher bacterial concentration, the cells were noticeable under the surface of the matrix (Figure 5C,D; shown by a red arrow). In addition, matrix porosity was determined by analysing the SEM images, and an ANOVA showed that there were no significant differences between the samples (Supplementary Table S6).
Figure 5. Examples of scanning electron microscopy (SEM) images of freeze-dried R2LC. All samples contain 10% lyoprotectant and were dried without an annealing step. (A) Sucrose with 109 CFU/mL; (B) Trehalose with 109 CFU/mL; (C) Sucrose with 1010 CFU/mL; (D) Trehalose with 1010 CFU/mL, bacterial cells embedded in the matrix shown by red arrows. All images have 1000× magnification.
Figure 5. Examples of scanning electron microscopy (SEM) images of freeze-dried R2LC. All samples contain 10% lyoprotectant and were dried without an annealing step. (A) Sucrose with 109 CFU/mL; (B) Trehalose with 109 CFU/mL; (C) Sucrose with 1010 CFU/mL; (D) Trehalose with 1010 CFU/mL, bacterial cells embedded in the matrix shown by red arrows. All images have 1000× magnification.
Applmicrobiol 03 00092 g005
The cake appearance, which was observed visually, was significantly affected by the lyoprotectant concentration and bacterial concentration (p < 0.001 and p = 0.008 respectively) according to a Kruskal–Wallis test (Table 4). In addition, Tukey’s post hoc tests showed that lower (109 CFU/mL) R2LC concentration and the highest lyoprotectant concentration (20%) promoted a partial or fully collapsed cake using both sucrose and trehalose as lyoprotectants (Table S2).
Table 4. Main effects of the experimental factors affecting cake appearance. p-values in bold indicate statistically significant effects.
Table 4. Main effects of the experimental factors affecting cake appearance. p-values in bold indicate statistically significant effects.
FactorStatisticdfp
Lyoprotectant type0.06910.792
Annealing0.14010.709
Lyoprotectant concentration23.9852<0.001
Bacterial concentration6.97910.008

3.2. Effect of Accelerated Storage on Water Content of Freeze-Dried R2LC

To investigate the effect of accelerated storage on water content, the samples were stored at 37 °C and water content was measured after 2 weeks. We observed that samples with the highest lyoprotectant concentration (20%) and lower concentration of bacteria (109 CFU/mL) had increased water content after storage, when using both sucrose and trehalose as lyoprotectants (ptukey < 0.001) (Table 5, Figure 6, and Table S8).
Table 5. Main effects and interactions of the experimental factors affecting water content of freeze-dried R2LC during accelerated storage. p-values in bold indicate statistically significant effects.
Table 5. Main effects and interactions of the experimental factors affecting water content of freeze-dried R2LC during accelerated storage. p-values in bold indicate statistically significant effects.
FactorsFpη2p
Lyoprotectant type1.9700.1630.015
Annealing0.0050.943<0.001
Lyoprotectant concentration (%)38.179<0.0010.372
Lyoprotectant × Annealing15.335<0.0010.106
Bacterial Concentration63.277<0.0010.329
Annealing × Bacterial Concentration3.4500.0660.026
Lyoprotectant concentration (%) × Bacterial Concentration9.938<0.0010.134
Figure 6. Accelerated storage: Effect of the different lyoprotectant types of sucrose (A,B) and trehalose (C,D) and interactions with lyoprotectant concentrations and bacterial concentrations on water content of freeze-dried R2LC. Datasets with different letters are significantly different (p < 0.01; data presented in A,C are compared and B,D are compared). (A,C), violet represents 20%, orange 15% and green 10% lyoprotectant concentration, respectively; (B,D), orange represents l09 CFU/mL and green represents 1010 CFU/mL R2LC.
Figure 6. Accelerated storage: Effect of the different lyoprotectant types of sucrose (A,B) and trehalose (C,D) and interactions with lyoprotectant concentrations and bacterial concentrations on water content of freeze-dried R2LC. Datasets with different letters are significantly different (p < 0.01; data presented in A,C are compared and B,D are compared). (A,C), violet represents 20%, orange 15% and green 10% lyoprotectant concentration, respectively; (B,D), orange represents l09 CFU/mL and green represents 1010 CFU/mL R2LC.
Applmicrobiol 03 00092 g006

3.3. Effects of Experimental Factors on Biological Properties of Lyophilized R2LC

The impact of the experimental factors on the biological outcomes of freeze-drying survival, metabolic activity, and storage stability was evaluated. We first investigated how well the bacteria survived the lyophilization process, and it was found that the type and concentration of lyoprotectant and annealing had an impact. All factors apart from bacterial concentration significantly affected the freeze-drying survival (p < 0.001) (Table 6). Also, all factors except lyoprotectant concentration significantly affected the metabolic activity of freeze-dried R2LC (p < 0.001) (Table 7). Post hoc analysis showed that sucrose resulted in significantly higher survival than trehalose (t = 7.007, ptukey < 0.001) (Figure 7 and Table S9). In addition, annealing had a positive effect when using sucrose but not trehalose as lyoprotectant (t = 8.292, ptukey < 0.001) (Figure 8E,F). A final observation was that the concentration of lyoprotectant had an impact on the survival, with 15% being most efficient for sucrose and 20% for trehalose (t = 4.133, ptukey = 0.003) (Figure 7A,B).
Table 6. Main effects and interactions of the experimental factors affecting freeze-drying survival of freeze-dried R2LC. p-values in bold indicate statistically significant effects.
Table 6. Main effects and interactions of the experimental factors affecting freeze-drying survival of freeze-dried R2LC. p-values in bold indicate statistically significant effects.
FactorsFpη2p
Lyoprotectant type49.097<0.0010.584
Annealing12.986<0.0010.271
Lyoprotectant concentration3.5680.0390.169
Bacterial concentration1.279 × 10−40.9913.654 × 10−6
Lyoprotectant × Annealing22.274<0.0010.389
Lyoprotectant × Lyoprotectant concentration5.3830.0090.235
Lyoprotectant × Bacterial concentration3.1880.0830.083
Annealing × Bacterial concentration3.8380.0580.099
Figure 7. Effect of lyoprotectant sucrose (A) and trehalose (B), with annealing (C), and without annealing (D) on freeze-drying survival. Datasets with different letters are significantly different (p < 0.01; data presented in A,B are compared and C,D are compared). (A,B), violet represents 20%, orange 15% and green 10% lyoprotectant concentration, respectively; (C,D), orange represents samples with sucrose and green represents trehalose as lyoprotectant.
Figure 7. Effect of lyoprotectant sucrose (A) and trehalose (B), with annealing (C), and without annealing (D) on freeze-drying survival. Datasets with different letters are significantly different (p < 0.01; data presented in A,B are compared and C,D are compared). (A,B), violet represents 20%, orange 15% and green 10% lyoprotectant concentration, respectively; (C,D), orange represents samples with sucrose and green represents trehalose as lyoprotectant.
Applmicrobiol 03 00092 g007
Furthermore, the metabolic activity of the freeze-dried R2LC was investigated and it was shown that sucrose gave a higher metabolic activity than trehalose (t = 43.608, ptukey < 0.001) (Figure 8, Table 7, and Table S10). In addition, using an annealing step had a positive impact when using sucrose (t = 16.428, ptukey < 0.001) but not trehalose (t = 0.159, ptukey = 0.999) as the lyoprotectant (Figure 8B,D). Additionally, a higher bacterial concentration gave an increased metabolic activity (t = 34.811, ptukey < 0.001) (Figure 8A,C).
Table 7. Main effects and interactions of the experimental factors affecting freeze-drying metabolic activity of freeze-dried R2LC. p-values in bold indicate statistically significant effects.
Table 7. Main effects and interactions of the experimental factors affecting freeze-drying metabolic activity of freeze-dried R2LC. p-values in bold indicate statistically significant effects.
FactorsFpη2p
Lyoprotectant type1901.639<0.0010.982
Annealing137.569<0.0010.797
Lyoprotectant concentration2.1500.1320.109
Bacterial concentration1211.809<0.0010.972
Lyoprotectant × Annealing132.329<0.0010.791
Annealing × Bacterial concentration47.846<0.0010.578
Lyoprotectant concentration × Bacterial concentration5.7080.0070.246
Figure 8. Effect of lyoprotectant, annealing, and bacterial concentration on metabolic activity. Datasets with different letters are significantly different (p < 0.01; data presented in A,C are compared and B,D are compared). (A,C), orange represents 109 CFU/mL and green represents 1010 CFU/mL R2LC; Figure 6B,D, orange represents samples with annealing step and green represents samples without annealing step.
Figure 8. Effect of lyoprotectant, annealing, and bacterial concentration on metabolic activity. Datasets with different letters are significantly different (p < 0.01; data presented in A,C are compared and B,D are compared). (A,C), orange represents 109 CFU/mL and green represents 1010 CFU/mL R2LC; Figure 6B,D, orange represents samples with annealing step and green represents samples without annealing step.
Applmicrobiol 03 00092 g008

3.4. Effect of Accelerated Storage Stability on Biological Properties

Storage stability of the freeze-dried R2LC samples was investigated after incubation at 37 °C (a temperature resulting in an accelerated decline in activity) for 2 weeks. As shown in Table 8, Table S11 and S12, both types of lyoprotectant and bacterial concentration had a significant impact on survival and metabolic activity. Post hoc Tukey tests revealed that sucrose gave significantly better survival (t = 4.412, ptukey < 0.001) and often more than 2 times higher metabolic activity (t = 2.444, ptukey = 0.033) than trehalose (Figure 9). Interestingly, 10–15% sucrose gave the best stability for the lower bacterial concentration, while 15–20% sucrose was better for the higher bacterial concentration (Figure 9A,C). Trehalose gave better stability for the highest bacterial concentration than for the lower concentration (Figure 9B,D). Furthermore, the survival was significantly lower for the trehalose-containing formulations compared to the formulations with sucrose.
Table 8. Main effects and interactions of the experimental factors affecting biological properties (A) storage survival and (B) metabolic activity of freeze-dried R2LC storage stability at week 2. p-values in bold indicate statistically significant effects.
Table 8. Main effects and interactions of the experimental factors affecting biological properties (A) storage survival and (B) metabolic activity of freeze-dried R2LC storage stability at week 2. p-values in bold indicate statistically significant effects.
A
FactorsFpη2p
Lyoprotectant type19.470<0.0010.357
Annealing3.1540.0840.083
Lyoprotectant concentration2.3240.1130.117
Bacterial concentration5.4450.0250.135
Lyoprotectant × Annealing7.9250.0080.185
Lyoprotectant × Lyoprotectant concentration3.6090.0380.171
Lyoprotectant × Bacterial concentration6.4630.0160.156
Annealing × Bacterial concentration3.0860.0880.081
Lyoprotectant concentration × Bacterial concentration9.728<0.0010.357
B
FactorsFpη2p
Lyoprotectant type5.9710.0330.352
Annealing1.0970.3170.091
Lyoprotectant concentration2.6750.1130.327
Bacterial concentration45.088<0.0010.804
Lyoprotectant × Bacterial concentration4.1330.0670.273
Lyoprotectant concentration × Bacterial concentration11.1840.0020.670
Figure 9. Evaluation of accelerated stability after 2 weeks. Effects of different factors and their interactions on survival (A,B) and metabolic activity (C,D) of freeze-dried R2LC. Datasets with different letters are significantly different (p < 0.01; data presented in A,B compared and C,D are compared).
Figure 9. Evaluation of accelerated stability after 2 weeks. Effects of different factors and their interactions on survival (A,B) and metabolic activity (C,D) of freeze-dried R2LC. Datasets with different letters are significantly different (p < 0.01; data presented in A,B compared and C,D are compared).
Applmicrobiol 03 00092 g009

3.5. Correlation between Physicochemical and Biological Outcomes

Finally, potential correlations between the physicochemical and biological outcomes were investigated. This analysis was exploratory and should be regarded as such. There was a positive correlation between freeze-drying survival and metabolic activity (Pearson’s r = 0.463, p < 0.001), as well as the physicochemical parameter aggregation correlating positively with metabolic activity (Pearson’s r = 0.503, p < 0.001) (Table 9, whilst Tg correlated negatively with both freeze-drying survival (Pearson’s r = −0.602, p = 0.002), and metabolic activity (Pearson’s r = −0.551, p = 0.005). In addition, correlations between physicochemical parameters were seen (Table 9).
Evaluation of the results from the stability study showed that survival and metabolic activity had a positive correlation (Pearson’s r = 0.798, p < 0.001), but there was no direct correlation between metabolic activity and survival with residual water content (%) (Table 10).

4. Discussion

Formulation and process parameters are known to play an important role in achieving freeze-dried probiotics with high viable counts, stability, and metabolic activity (vitality). Many studies of the impact of different lyoprotectants and process parameters have previously been carried out [6,8,36,37,38], but mostly they have focused on the evaluation of either biological or physicochemical properties of the freeze-dried product. We therefore decided to carry out a comprehensive investigation of the effects of various production factors on both physicochemical and biological properties of freeze-dried Limosilactobacillus reuteri R2LC. The freeze-drying process includes a wide range of variables and our goal was to use a standard method and evaluate a limited number of factors representing different aspects of the process. These included (i) the lyoprotectant for which both the type of protecting sugar and its concentration were evaluated; (ii) the concentration of bacteria; and (iii) an annealing step in the freeze-drying program (Figure 1).
The biological properties, i.e., freeze-drying survival, metabolic activity, and storage stability, are the main attributes that contribute to the quality and potency of the probiotic product. Type of sugar was the only factor that had a significant effect on all three quality attributes (Table 6, Table 7 and Table 8) and sucrose performed better overall than trehalose (Figure 7, Figure 8 and Figure 9). Contrary to this, there are several publications that describe that trehalose provides a better protection of freeze-dried organisms and proteins than sucrose [39,40,41,42,43]. The reason for this discrepancy is not known, but it may be an effect specific to L. reuteri or the strain used (R2LC). The composition of lyoprotectants could be more complex than the pure sugar formulations used in the present study and many researchers have achieved good results using combinations of different protectants such as gelatine, skim milk, glucose, sucrose, and trehalose [44,45].
Lyoprotectant concentration also affected the biological properties, but the only significant effect was seen on freeze-drying survival (Table 6, Table 7 and Table 8). However, the effect of sucrose concentration varied greatly and interacted with the bacterial concentration (Figure 9). Using 10% sucrose gave a poor stability of the highest concentration of bacteria while 20% sucrose worked well for this bacterial concentration but gave very poor stability and collapsed cakes when used in combination with the low concentration of bacteria (Figure 9, Table S7). Overall, 15 or 20% sucrose combined with high bacterial concentration gave the best stability. This indicates that a high concentration of sucrose is needed to protect a high concentration of bacteria, but also that a high concentration of bacteria can stabilize the cake with a high concentration of sucrose. It has previously been shown that different concentrations and types of lyoprotectants affect the biological parameters. Jawan et al. (2022) investigated the effect of different types (monosaccharides, disaccharides, sugar alcohol, complex media) and concentrations (5, 10, and 20%) of lyoprotectants on cell viability and antimicrobial activity of freeze-dried Lactococcus lactis Gh1, and they observed that galactose resulted in the highest freeze-drying survival followed by trehalose and peptone. Storage stability was also investigated and viability varied significantly between different lyoprotectant types and concentrations [46].
The products with high bacterial concentration generally had higher metabolic activity than the products with low concentration (diluted to the same concentration in the assay). Interestingly, both a high concentration of bacteria and high metabolic activity correlated with aggregation of the bacteria and, to the best of our knowledge, this type of correlation has not previously been reported. We also observed a positive effect of annealing on the biological outcomes when using sucrose but not trehalose as a lyoprotectant. This is in accordance with the effect of annealing on freeze-dried Lactobacillus acidophilus previously described by Ekdawi-Sever et al. [22].
This work highlights the importance of optimizing the lyoprotectant, its balance with the bacterial concentration, and an evaluation of annealing as part of the freeze-drying process. Several factors affect the quality of the freeze-dried bacteria and many of these effects can also be strain-specific. To achieve a product with sufficient and consistent quality, knowledge about the strain selected for the product concept is therefore key in developing a production method that is specifically optimized for the intended product as well as the intended application and indication.

Supplementary Materials

The following supporting information can be downloaded at: https://www.mdpi.com/article/10.3390/applmicrobiol3040092/s1, Table S1: DOE: Full factorial screening with 24 independent runs; Table S2: Description of the cake appearance and their corresponding scoring numbers; Table S3. Tukey post-hoc tests: effects and interactions of the factors on water content of freeze-dried R2LC; Table S4. Tukey post-hoc tests: effects and interactions of the factors on Tg of freeze-dried R2LC; Table S5. Tukey post-hoc tests: effects and interactions of the factors on aggregation of freeze-dried R2LC; Table S6. Porosity of freeze-dried R2LC and an ANOVA and Tukey post-hoc tests: effects and interactions of the factors on porosity of freeze-dried R2LC; Table S7. Tukey post-hoc tests: effects and interactions of the factors on cake appearance of freeze-dried R2LC; Table S8. Accelerated stability- Tukey post-hoc tests: effects and interactions of the factors on water content of freeze-dried R2LC; Table S9. Post-Hoc test to evaluate the effect of all variables on freeze-drying survival of freeze-dried R2LC; Table S10. Post-Hoc test to evaluate the effect of all variables on freeze-drying metabolic activity of freeze-dried R2LC; Table S11. Post-Hoc test to evaluate the effect of accelerated storage stability (week 2) on survival; Table S12. Post-Hoc test to evaluate the effect of accelerated storage stability (week 2) on metabolic activity.

Author Contributions

Conceptualization, N.T., L.R., A.M.F. and S.R.; Methodology, N.T., E.S.C., S.K., A.M.F. and S.R.; Formal analysis, N.T., D.T.O. and E.S.C.; Investigation, N.T., Z.G., D.T.O. and S.K.; Resources, A.M.F. and S.R.; Data curation, N.T., E.S.C. and S.R.; Writing—original draft, N.T.; Writing—review & editing, D.T.O., E.S.C., L.R., A.M.F. and S.R.; Visualization, N.T.; Supervision, L.R. and S.R.; Project administration, N.T.; Funding acquisition, L.R., A.M.F. and S.R. All authors have read and agreed to the published version of the manuscript.

Funding

Ilya Pharma AB is acknowledged for funding this research project. This research was also financed through the Competence Centre NextBioForm, funded by the Vinnova Swedish Governmental Agency for Innovation, and the Swedish Research Council under grant number 2018-04730.

Data Availability Statement

Data are contained within the article and supplementary materials.

Acknowledgments

The authors wish to thank Evelina Vågesjö for support and valuable comments on the manuscript, and Zhanar Myktybekova and Yanhong Pang for experimental support.

Conflicts of Interest

SR is shareholder of Ilya Pharma. NT, LR and SK have stock options and are employees of Ilya Pharma.

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Table 9. Pearson’s correlations between physicochemical and biological outcomes. Statistically significant values (p < 0.05) are highlighted with bold figures.
Table 9. Pearson’s correlations between physicochemical and biological outcomes. Statistically significant values (p < 0.05) are highlighted with bold figures.
Pearson’s Correlations
Pearson’s rp
Metabolic activityFD survival0.463<0.001
Metabolic activityAggregation0.503<0.001
Metabolic activityPorosity0.2820.181
Metabolic activityWater content0.0630.770
Metabolic activityGlass transition temperature−0.5510.005
Metabolic activityCake appearance−0.1180.426
FD survivalAggregation0.0560.707
FD survivalPorosity0.3520.091
FD survivalWater content0.2030.341
FD survivalGlass transition temperature−0.6020.002
FD survivalCake appearance0.0450.759
AggregationPorosity0.2330.273
AggregationWater content−0.4320.035
AggregationGlass transition temperature0.2540.232
AggregationCake appearance−0.3060.035
PorosityWater content−0.2140.316
PorosityGlass transition temperature−0.1420.508
PorosityCake appearance−0.0880.682
Water contentGlass transition temperature−0.5370.007
Water contentCake appearance0.6130.001
Glass transition temperatureCake appearance−0.1240.564
Table 10. Pearson’s correlations between physicochemical and biological properties after the accelerated stability study. Statistically significant values (p < 0.05) are highlighted with bold figures.
Table 10. Pearson’s correlations between physicochemical and biological properties after the accelerated stability study. Statistically significant values (p < 0.05) are highlighted with bold figures.
Pearson’s rp
Metabolic activityWater content−0.1740.143
Metabolic activity Survival0.798<0.001
Water contentSurvival−0.0540.522
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Tyagi, N.; Gidlöf, Z.; Osanlóo, D.T.; Collier, E.S.; Kadekar, S.; Ringstad, L.; Fureby, A.M.; Roos, S. The Impact of Formulation and Freeze Drying on the Properties and Performance of Freeze-Dried Limosilactobacillus reuteri R2LC. Appl. Microbiol. 2023, 3, 1370-1387. https://doi.org/10.3390/applmicrobiol3040092

AMA Style

Tyagi N, Gidlöf Z, Osanlóo DT, Collier ES, Kadekar S, Ringstad L, Fureby AM, Roos S. The Impact of Formulation and Freeze Drying on the Properties and Performance of Freeze-Dried Limosilactobacillus reuteri R2LC. Applied Microbiology. 2023; 3(4):1370-1387. https://doi.org/10.3390/applmicrobiol3040092

Chicago/Turabian Style

Tyagi, Nisha, Zandra Gidlöf, Daniel Tristan Osanlóo, Elizabeth S. Collier, Sandeep Kadekar, Lovisa Ringstad, Anna Millqvist Fureby, and Stefan Roos. 2023. "The Impact of Formulation and Freeze Drying on the Properties and Performance of Freeze-Dried Limosilactobacillus reuteri R2LC" Applied Microbiology 3, no. 4: 1370-1387. https://doi.org/10.3390/applmicrobiol3040092

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