J Cosmet Med 2019; 3(2): 86-93
Published online December 31, 2019
Seungwon Chung, MS1, Hana Kwon, MS2, Namsoo Peter Kim, PhD1,2
1Department of Metallurgical Materials and Biomedical Engineering, The University of Texas at El Paso, El Paso, TX, United States
2Center for Printing Materials Certification, The University of Texas at El Paso, El Paso, TX, United States
Correspondence to :
Namsoo Peter Kim
E-mail: nkim@utep.edu
© Korean Society of Korean Cosmetic Surgery & Medicine
Background: Extracellular matrix (ECM) has been broadly applied and shown great promise in medical applications. ECM products should be used after decellularization and purification. Supercritical carbon dioxide treatment is of particular interest for purifying ECM due to its medical availability and rapid process speed. However, it is not fully researched for treatment of biomaterials for tissue engineering. Therefore, we investigated the optimal conditions of supercritical carbon dioxide processing at different extracting parameters in porcine adipose tissue.
Objective: We aimed to identify the optimal supercritical extracting conditions to produce non-cytotoxic and sterile decellularized extracellular matrix (DE-ECM) for regeneration therapeutics.
Methods: The three-day dual treatment including enzymatic decellularization and supercritical fluid extraction of pork adipose tissue was performed. Two protocols using different extracting parameters were applied to evaluate the influence of extracting pressure and temperature on the extraction yield, DNA concentration, and remaining collagen in product.
Results: Yield rate increased when high temperature or pressure was applied and pre-enzyme treatment had higher yield rate percent than pre-supercritical processing. Nearly 90% DNA was removed from the pre-enzyme sample when extracted at 3.04×107 Pa and 30°C±5°C. The pre-enzyme process had efficient extracting ability at each temperature and pressure and the remaining collagen steadily decreased with increase in extracting pressure and temperature. At the lowest temperature (20°C±5°C) and pressure (1.01×107 Pa), remaining collagen was 75.74%±1.83%. Supercritical extraction technology can produce DE-ECM eliminating DNA content efficiently and the remaining proper collagen amount successfully.
Conclusion: This study evaluated the feasibility of utilizing supercritical extraction technology in bio-materials and was proven to be is successful. Through controlling the extracting pressure and temperature, this technology has a potential for DE-ECM mass production, which can be useful as tissue regeneration therapeutics as well new drug delivery paradigm.
Keywords: enzyme decellularization, extracellular matrix, regeneration therapeutics, supercritical extraction process
Tissue engineering (TE) has been proposed for in vitro production of artificial tissues and organs and related issues have attracted attention in the medical field. Currently, various biopolymers and materials for regeneration therapy are being researched. However, there are side effects such as in vivo tissue damage due to pH decrease in the implanted site and worsening biocompatibility with time. Therefore, natural materials with high degree of biocompatibility as well as the ability to direct cellular proliferation and constructive tissue remodeling have attracted attention from researchers and showed great promise in medical applications [1,2]. Especially, biological scaffold including extracellular matrix (ECM) has been broadly applied in medical field [3-6]. The ECM is a complex matrix surrounded by cells and take structural and biochemical supporting functions from bioactive ingredients such as collagen, elastin, glycosaminoglycans (GAGs), growth factors, and cytokine [7,8]. However, traditional decellularization method generally use chemical detergents that are cytotoxic and can damage ECM and has disadvantages such as high cost and being time-consuming [9-12]. As shown in Table 1, most decellularization methods can transform the 3-dimensional biostructure of tissues related to mechanical properties; also, the chemical detergents and acids can remain inside the tissue after processing and cause substantial adverse immune effects [13-22].
Table 1 . Summary of decellularization agents and technique for producing decellularized extracellular matrix tissue
Agent/technique | Mechanism | Effect | Reference |
---|---|---|---|
Acids and base | Solubilize cytoplasmic components of cells and tend to denature proteins. | Decrease collagen amount and GAG. | [15,16] |
Hypotonic and hypertonic | Occur Cell lysis by osmotic shock and disrupt DNA-protein interactions. | Non-effective in removing cellular residue. | [17] |
Tributyl phosphate | Form stable complexes with metals and disrupt protein-protein interactions. | Mixed results with efficacy dependent on tissue, dense tissues lost collagen. | [18] |
Nucleases | Catalyze the hydrolysis of ribonucleotide. | Difficult to remove from the tissue and invoke an immune response. | [19] |
Freezing | Intracellular ice crystals disrupt cell membrane. | Ice crystal formation disrupts or fracture in product. | [20] |
Electroporation | Pulsed electrical fields disrupt cell membranes. | Electrical field oscillation disrupts ECM structure. | [21] |
Agitation | Lyse cells and facilitate chemical exposure. | Aggressive agitation or sonication damages ECM. | [21] |
Perfusion | Facilitate chemical exposure and removal of cellular material. | Pressure associated with perfusion disrupt ECM. | [22] |
GAG, glycosaminoglycans; ECM, extracellular matrix.
In this study, two decellularizing and purifying protocols were used to produce medically available decellularized extracellular matrix (DE-ECM). Pork adipose tissue was used because it is an abundant source of useful particles such as collagen, peptides, and cytokines [23,24]. Decellularization was performed with enzyme solutions that separate proteins and eliminate lipid or cellular contents [25-27]. To overcome time-consuming limitations of chemical decellularization, the supercritical extraction by carbon dioxide (SC-CO2) was applied as additional purification process [28]. Supercritical fluid is achieved when the substance is above critical point and cannot be defined as liquid or gas. It has particular properties—selectivity, expeditiousness, and high degree of dissolution ability—because it has intermediate properties of viscosity and density of gas and liquid. Using carbon dioxide as the main solvent enhances extraction efficiency since it is non-corrosive, non-flammable, and nontoxic and has short process time and high efficiency. SC-CO2 has variety of application in foods and biomaterial because the pressure and temperature at supercritical state have a moderate value [29-32]. This study focuses on the medically available synthesis of bi compatible DE-ECM applying SC-CO2 and investigates the optimal extracting conditions for elimination of DNA content and useless components.
The produced DE-ECM was decellularized with enzymatic solution and supercritical extracted with CO2 (SC-CO2). The experimental processes are summarized in Fig. 1. In brief, the three-day, cost-effective, and non-toxic procedure involved enzymatic decellularization and supercritical fluid extraction treatment. Two types of treatment protocols were followed. According to the first treatment method, the supercritical extraction was carried out after enzyme decellularization process (pre-enzyme treatment). According to the second treatment, the enzyme process was carried out after supercritical extraction (pre-supercritical treatment). Different extracting parameters were applied for these experiments; extractions were carried out at different pressures and temperature to evaluate the influence of pressure and temperature on the extraction yield, DNA concentration, and remaining collagen amount. All the decreased weight data were recorded.
Pork adipose tissue was used to produce DE-ECM. The raw pork was obtained from a local grocery store and kept in the freezer to avoid degradation. The comminution of the raw adipose tissue was harvested using an electric grinder and each tissue was cut into small pieces of different thickness (T1, 1.9×10-3 m; T2, 5.7×10-3 m; and T3, 9.5×10-3 m). The raw adipose tissues prepared were of identical volume, 3.8×10-7 m3. It was possible to control volume of all the tissues.
The supercritical extractions were carried out to remove DNA components and purify by non-toxic and non-destructive way by the apparatus described in Fig. 2 (OCO-LABS, Redway, CA, USA). The extractor includes an extraction vessel with maximum operating pressure 5.07×107 Pa. Pressure within the extraction vessel (described in Fig. 2C) was kept constant by monitoring via a gas gauge and the temperature was set by internal sensors. The extracted ingredients were collected in the flask (Fig. 2D) by depressurizing after 30 minutes. The extractions were conducted in 30 minute cycles to give enough time for the supercritical fluid to dissolve the target components. Carbon dioxide was utilized as the solvent material, which has medically available features. To eliminate the residual extracted ingredients on the surface, tissues were purified with deionized water during 180 minutes. Different extracting parameters were applied in order to compare extraction efficiency (temperature: 20°C±5°C, 30°C±5°C, and 40°C±5°C; pressure: 1.01×107 Pa, 2.03×107 Pa, and 3.04×107 Pa). The produced tissue mass was measured before and after the extraction as well. The experiments were conducted thrice in each condition to investigate the effect of extracting variables.
Decellularization was performed via the three-day protocol. The adipose tissues were subjected to chemical decellularization with enzymatic solutions and deionized water. The tissues were submerged into a 1:1 solution of 0.05% Trypsin-EDTA and 0.032 M deoxycholic acid (Sigma-Aldrich, St. Louis, MO, USA). The adipose tissues were then thoroughly submerged in a 1:1 solution of 0.02% Trypsin and deoxycholic acid at 20°C and incubated overnight for 48 hours. This enzymatic digestive solution dissociates protein and adherent cells. The amount of solution used was five times the tissue mass. Subsequently, the tissues were rinsed with 30 ml deionized water. Temperature and pH (approximately pH 7) were measured to determine whether other accidental chemical reactions occurred. Following a washing course in deionized water, the tissues were transferred into the solutions containing Triton X-100 (Sigma-Aldrich) and deionized water for six hours. The tissue was then put in deionized water to re-rinse for six hours. Finally, the adipose segments were mechanically compressed for dehydration and then stored at 4°C.
To investigate the DNA concentration after treatment, Pico-green dsDNA assay (Invitrogen, Camarillo, CA, USA) was performed [33]. Since it is a colorimetric procedure, the test materials for analysis must be free from particulate materials such as cell debris and insoluble ECM fragments. To expose DNA contents, acid–pepsin digestion was applied to the tissues. They were submerged in 0.1 mg pepsin/ml 0.5 M acetic acid, which works as an enzyme for eliminating the terminal non-helical telopeptides to release the ingredients into solution. After pre-experiment to prepare samples for evaluation, DNA concentration was measured by VERSA Max Tunable Microplate Reader (Molecular Devices Corp., San Jose, CA, USA).
The amount of remaining collagen after treatment was evaluated by assaying soluble collagen with a sircol collagen assay (SCA) kit (Biocolor Ltd., County Antrim, UK). Briefly, SCA is a colorimetric procedure therefore tissue were freed of cell debris and insoluble ECM fragments. The test samples (10 mg each) were homogenized in acetic acid with pepsin. Each sample was incubated at 4°C and separated into pellet and supernatant by centrifugation. Sircol dye reagent that binds to collagen was applied to each sample. After centrifugation, an alkaline reagent was added to the pellet. The absorbance was measured at 540 nm wavelength on a microplate reader.
A non-toxic, cost-effective, and short DE-ECM processing methodology including supercritical extraction and enzymatic decellularization was established. Adipose tissues were treated with different process protocols (pre-enzyme or pre-supercritical process). After the completed processes, the white colored matrix with significantly decreased mass was collected (Fig. 3). Macroscopically, the raw adipose tissue size was different according to its thickness because of mechanical compression, but the produced DE-ECM had a similar appearance with it being whiter than the raw tissue after the entire processes.
The yield rate of DE-ECM with different extracting parameters was compared (Table 2). Adipose tissues with three different thicknesses were processed via the pre-enzyme or pre-supercritical process at three different pressures and two different temperatures. The tissue weight before and after processing was measured. It was found that yield rate depends on the extracting temperature and pressure. Fig. 4 shows the influence of extracting pressure and temperature on yield rate. The yield rates at 40°C±5°C using different protocols and at different pressures were as follows: pre-enzyme process at 1.01×107 Pa: 25.13%±4.02%, 2.03×107 Pa: 40.87%±3.09%, and 3.04×107 Pa: 45.62%±3.75%; pre-supercritical process at 1.01×107 Pa: 14.40%±3.54%, 2.03×107 Pa: 19.31%±5.95%, and 3.04×107 Pa: 21.47%±5.58%. Similarly, the yield rates at 30°C±5°C were: pre-enzyme process at 1.01×107 Pa: 18.34%±7.46%, 2.03×107 Pa: 26.58%±4.35%, and 3.04×107 Pa: 34.04%±4.04%; pre-supercritical process at 1.01×107 Pa: 4.85%±3.04%, 2.03×107 Pa: 15.49%±2.47%, and 3.04×107 Pa: 21.74%±8.12%. Yield rate increased when high temperature or pressure was applied. Furthermore, pre-enzyme treatment had higher processed DE-ECM yield rate percent than that of pre-supercritical treatment. The maximum yield rate observed was nearly 46% at 3.04×107 Pa pressure and 40°C±5°C temperature using the pre-enzyme process.
Table 2 . Extraction yield of decellularized extracellular matrix product with different extraction condition
Adipose tissue | Process | Pressure (×107 Pa) | Temperature (±5°C) | Weight of original mass (g) | Weight of product (g) |
---|---|---|---|---|---|
1 | PE | 1.01 | 30 | 0.21 | 0.17 |
40 | 0.20 | 0.16 | |||
2.03 | 30 | 0.22 | 0.15 | ||
40 | 0.25 | 0.15 | |||
3.04 | 30 | 0.23 | 0.15 | ||
40 | 0.20 | 0.09 | |||
PS | 1.01 | 30 | 0.15 | 0.15 | |
40 | 0.24 | 0.20 | |||
2.03 | 30 | 0.24 | 0.19 | ||
40 | 0.19 | 0.14 | |||
3.04 | 30 | 0.20 | 0.14 | ||
40 | 0.17 | 0.12 | |||
2 | PE | 1.01 | 30 | 0.47 | 0.37 |
40 | 0.45 | 0.34 | |||
2.03 | 30 | 0.61 | 0.47 | ||
40 | 0.49 | 0.29 | |||
3.04 | 30 | 0.52 | 0.33 | ||
40 | 0.64 | 0.38 | |||
PS | 1.01 | 30 | 0.44 | 0.35 | |
40 | 0.43 | 0.38 | |||
2.03 | 30 | 0.46 | 0.39 | ||
40 | 0.53 | 0.46 | |||
3.04 | 30 | 0.45 | 0.36 | ||
40 | 0.42 | 0.35 | |||
3 | PE | 1.01 | 30 | 0.62 | 0.56 |
40 | 0.62 | 0.44 | |||
2.03 | 30 | 0.60 | 0.42 | ||
40 | 0.62 | 0.35 | |||
3.04 | 30 | 0.70 | 0.48 | ||
40 | 0.60 | 0.35 | |||
PS | 1.01 | 30 | 0.67 | 0.64 | |
40 | 0.70 | 0.60 | |||
2.03 | 30 | 0.89 | 0.80 | ||
40 | 0.62 | 0.51 | |||
3.04 | 30 | 0.78 | 0.66 | ||
40 | 0.67 | 0.55 |
Adipose tissue 1: thickness 1.9×10-3 m, Adipose tissue 2: thickness 5.7×10-3 m, Adipose tissue 3: thickness 9.5×10-3 m.
PE, pre-enzyme process; PS, pre-supercritical process.
The DNA content in DE-ECM tissues was compared with that of native adipose tissue (measured average DNA concentration: 0.065 µg/ml). Fig. 5 shows the concentration of remaining DNA after decellularization and supercritical extraction at different temperatures and pressures (DNA concentration of DE-ECM tissues produced using pre-enzyme process at 40°C±5°C—1.01×107 Pa: 49.23%±3.48%, 2.03×107 Pa: 24.62%±4.35%, and 3.04×107 Pa: 10.77%±3.43%; DNA concentration of DE-ECM tissues using produced pre-supercritical process at 40°C±5°C—1.01×107 Pa: 61.54%±1.10%, 2.03×107 Pa: 56.92%±2.39%, and 3.04×107 Pa: 27.69%±1.31%; DNA concentration of DE-ECM tissues produced using pre-enzyme process at 30°C±5°C—1.01×107 Pa: 24.62%±5.52%, 2.03×107 Pa: 18.46%±3.36%, and 3.04×107 Pa: 9.23%±0.38%; DNA concentration of DE-ECM tissues using produced pre-supercritical process at 30°C±5°C—1.01×107 Pa: 38.46%±6.16%, 2.03×107 Pa: 30.77%±10.22%, and 3.04×107 Pa: 21.54%±3.18%). DNA concentration of DE-ECM tissues extracted using pre-enzyme process at 3.04×107 Pa and 30°C±5°C was the lowest, with nearly 90% DNA being removed. This result indicates that the different kinds of ingredients, which contain different value of DNA contents, are extracted because of solubility difference.
The influence of temperature and pressure on the collagen concentration is presented in Fig. 6. The collagen amount in DE-ECM tissues were compared to those in original native adipose tissue (measured collagen content: ~0.90±0.03 µg/ml). Fig. 6 indicates that collagen amount steadily decreased with increase in extracting pressure from 1.01×107 to 3.04×107 Pa. Moreover, DE-ECM tissues produced at 20°C±5°C had more collagen than the tissues processed at 30°C±5°C and 40°C±5°C. At 40°C±5°C, the collagen content of DE-ECM were 24.88%±2.44%, 14.08%±2.10%, and 8.11%±6.87% at 1.01×107 Pa, 2.03×107 Pa, and 3.04×107 Pa, respectively. At 30°C±5°C, they were 33.97%±0.67%, 22.59%±0.79%, and 17.72%±4.86% at 1.01×107, 2.03×107, and 3.04×107 Pa, respectively. Similarly, at 20°C±5°C, they were 75.74%±1.83%, 43.17%±3.57%, and 32.11%±4.78% at 1.01×107 Pa, 2.03×107 Pa, and 3.04×107 Pa, respectively.
The purpose of this study was to produce biocompatible DE-ECM by a cost-effective, short, and non-toxic process. Supercritical fluid extraction with carbon dioxide (SC-CO2) and decellularization with enzymatic solutions were applied to treat DE-ECM. The combination of SC-CO2 and enzyme treatment produced DE-ECM samples in 70 hours cost-effectively and satisfactorily eliminated DNA. To increase solvent solubility, different experiment parameters such as extracting pressure and temperature were investigated by increasing the solvent density [34,35]. However, in a different aspect, temperature had a severe effect on the collagen composition of DE-ECM since collagen is vulnerable at high temperature [36,37]. DNA analysis showed that extraction using pre-enzyme process at 30°C±5°C and 3.04×107 Pa was the optimal condition to decrease DNA concentration, that is, DNA concentration decreased from 0.065 µg/ml of original adipose tissue to 0.006 µg/ml of produced DE-ECM. Collagen is a critical element in pharmaceutical and biomedical industries and has an important role in tissue and organ formation due to ultimate biocompatibility with the immune system. The collagen analysis result shows that DE-ECM produced at optimal extraction conditions using the pre-enzyme process had 0.16 µg/ml collagen; 17.72%. Thus, high pressure and low temperature are the effective variables to produce biocompatible DE-ECM. Application of supercritical fluid extraction and enzyme decellularization process proves that cost-effective, non-toxic, and less time-consuming production of medically available DE-ECM is possible without using any unnecessary chemicals that damages the biostructure. Moreover, controlling pressure and temperature provides optimal biocompatibility and has a potential usage of supercritical fluid extraction in DE-ECM mass production, as it is a rapid process. This study evaluated the feasibility of utilizing supercritical extraction technology in biomaterials and it was proven successful. Moreover, medically available DE-ECM can be utilized in tissue regeneration therapeutics including medical pad with drugs as well as new drug delivery paradigm.
The authors have nothing to disclose.
J Cosmet Med 2019; 3(2): 86-93
Published online December 31, 2019 https://doi.org/10.25056/JCM.2019.3.2.86
Copyright © Korean Society of Korean Cosmetic Surgery & Medicine.
Seungwon Chung, MS1, Hana Kwon, MS2, Namsoo Peter Kim, PhD1,2
1Department of Metallurgical Materials and Biomedical Engineering, The University of Texas at El Paso, El Paso, TX, United States
2Center for Printing Materials Certification, The University of Texas at El Paso, El Paso, TX, United States
Correspondence to:Namsoo Peter Kim
E-mail: nkim@utep.edu
Background: Extracellular matrix (ECM) has been broadly applied and shown great promise in medical applications. ECM products should be used after decellularization and purification. Supercritical carbon dioxide treatment is of particular interest for purifying ECM due to its medical availability and rapid process speed. However, it is not fully researched for treatment of biomaterials for tissue engineering. Therefore, we investigated the optimal conditions of supercritical carbon dioxide processing at different extracting parameters in porcine adipose tissue.
Objective: We aimed to identify the optimal supercritical extracting conditions to produce non-cytotoxic and sterile decellularized extracellular matrix (DE-ECM) for regeneration therapeutics.
Methods: The three-day dual treatment including enzymatic decellularization and supercritical fluid extraction of pork adipose tissue was performed. Two protocols using different extracting parameters were applied to evaluate the influence of extracting pressure and temperature on the extraction yield, DNA concentration, and remaining collagen in product.
Results: Yield rate increased when high temperature or pressure was applied and pre-enzyme treatment had higher yield rate percent than pre-supercritical processing. Nearly 90% DNA was removed from the pre-enzyme sample when extracted at 3.04×107 Pa and 30°C±5°C. The pre-enzyme process had efficient extracting ability at each temperature and pressure and the remaining collagen steadily decreased with increase in extracting pressure and temperature. At the lowest temperature (20°C±5°C) and pressure (1.01×107 Pa), remaining collagen was 75.74%±1.83%. Supercritical extraction technology can produce DE-ECM eliminating DNA content efficiently and the remaining proper collagen amount successfully.
Conclusion: This study evaluated the feasibility of utilizing supercritical extraction technology in bio-materials and was proven to be is successful. Through controlling the extracting pressure and temperature, this technology has a potential for DE-ECM mass production, which can be useful as tissue regeneration therapeutics as well new drug delivery paradigm.
Keywords: enzyme decellularization, extracellular matrix, regeneration therapeutics, supercritical extraction process
Tissue engineering (TE) has been proposed for in vitro production of artificial tissues and organs and related issues have attracted attention in the medical field. Currently, various biopolymers and materials for regeneration therapy are being researched. However, there are side effects such as in vivo tissue damage due to pH decrease in the implanted site and worsening biocompatibility with time. Therefore, natural materials with high degree of biocompatibility as well as the ability to direct cellular proliferation and constructive tissue remodeling have attracted attention from researchers and showed great promise in medical applications [1,2]. Especially, biological scaffold including extracellular matrix (ECM) has been broadly applied in medical field [3-6]. The ECM is a complex matrix surrounded by cells and take structural and biochemical supporting functions from bioactive ingredients such as collagen, elastin, glycosaminoglycans (GAGs), growth factors, and cytokine [7,8]. However, traditional decellularization method generally use chemical detergents that are cytotoxic and can damage ECM and has disadvantages such as high cost and being time-consuming [9-12]. As shown in Table 1, most decellularization methods can transform the 3-dimensional biostructure of tissues related to mechanical properties; also, the chemical detergents and acids can remain inside the tissue after processing and cause substantial adverse immune effects [13-22].
Table 1 . Summary of decellularization agents and technique for producing decellularized extracellular matrix tissue.
Agent/technique | Mechanism | Effect | Reference |
---|---|---|---|
Acids and base | Solubilize cytoplasmic components of cells and tend to denature proteins. | Decrease collagen amount and GAG. | [15,16] |
Hypotonic and hypertonic | Occur Cell lysis by osmotic shock and disrupt DNA-protein interactions. | Non-effective in removing cellular residue. | [17] |
Tributyl phosphate | Form stable complexes with metals and disrupt protein-protein interactions. | Mixed results with efficacy dependent on tissue, dense tissues lost collagen. | [18] |
Nucleases | Catalyze the hydrolysis of ribonucleotide. | Difficult to remove from the tissue and invoke an immune response. | [19] |
Freezing | Intracellular ice crystals disrupt cell membrane. | Ice crystal formation disrupts or fracture in product. | [20] |
Electroporation | Pulsed electrical fields disrupt cell membranes. | Electrical field oscillation disrupts ECM structure. | [21] |
Agitation | Lyse cells and facilitate chemical exposure. | Aggressive agitation or sonication damages ECM. | [21] |
Perfusion | Facilitate chemical exposure and removal of cellular material. | Pressure associated with perfusion disrupt ECM. | [22] |
GAG, glycosaminoglycans; ECM, extracellular matrix..
In this study, two decellularizing and purifying protocols were used to produce medically available decellularized extracellular matrix (DE-ECM). Pork adipose tissue was used because it is an abundant source of useful particles such as collagen, peptides, and cytokines [23,24]. Decellularization was performed with enzyme solutions that separate proteins and eliminate lipid or cellular contents [25-27]. To overcome time-consuming limitations of chemical decellularization, the supercritical extraction by carbon dioxide (SC-CO2) was applied as additional purification process [28]. Supercritical fluid is achieved when the substance is above critical point and cannot be defined as liquid or gas. It has particular properties—selectivity, expeditiousness, and high degree of dissolution ability—because it has intermediate properties of viscosity and density of gas and liquid. Using carbon dioxide as the main solvent enhances extraction efficiency since it is non-corrosive, non-flammable, and nontoxic and has short process time and high efficiency. SC-CO2 has variety of application in foods and biomaterial because the pressure and temperature at supercritical state have a moderate value [29-32]. This study focuses on the medically available synthesis of bi compatible DE-ECM applying SC-CO2 and investigates the optimal extracting conditions for elimination of DNA content and useless components.
The produced DE-ECM was decellularized with enzymatic solution and supercritical extracted with CO2 (SC-CO2). The experimental processes are summarized in Fig. 1. In brief, the three-day, cost-effective, and non-toxic procedure involved enzymatic decellularization and supercritical fluid extraction treatment. Two types of treatment protocols were followed. According to the first treatment method, the supercritical extraction was carried out after enzyme decellularization process (pre-enzyme treatment). According to the second treatment, the enzyme process was carried out after supercritical extraction (pre-supercritical treatment). Different extracting parameters were applied for these experiments; extractions were carried out at different pressures and temperature to evaluate the influence of pressure and temperature on the extraction yield, DNA concentration, and remaining collagen amount. All the decreased weight data were recorded.
Pork adipose tissue was used to produce DE-ECM. The raw pork was obtained from a local grocery store and kept in the freezer to avoid degradation. The comminution of the raw adipose tissue was harvested using an electric grinder and each tissue was cut into small pieces of different thickness (T1, 1.9×10-3 m; T2, 5.7×10-3 m; and T3, 9.5×10-3 m). The raw adipose tissues prepared were of identical volume, 3.8×10-7 m3. It was possible to control volume of all the tissues.
The supercritical extractions were carried out to remove DNA components and purify by non-toxic and non-destructive way by the apparatus described in Fig. 2 (OCO-LABS, Redway, CA, USA). The extractor includes an extraction vessel with maximum operating pressure 5.07×107 Pa. Pressure within the extraction vessel (described in Fig. 2C) was kept constant by monitoring via a gas gauge and the temperature was set by internal sensors. The extracted ingredients were collected in the flask (Fig. 2D) by depressurizing after 30 minutes. The extractions were conducted in 30 minute cycles to give enough time for the supercritical fluid to dissolve the target components. Carbon dioxide was utilized as the solvent material, which has medically available features. To eliminate the residual extracted ingredients on the surface, tissues were purified with deionized water during 180 minutes. Different extracting parameters were applied in order to compare extraction efficiency (temperature: 20°C±5°C, 30°C±5°C, and 40°C±5°C; pressure: 1.01×107 Pa, 2.03×107 Pa, and 3.04×107 Pa). The produced tissue mass was measured before and after the extraction as well. The experiments were conducted thrice in each condition to investigate the effect of extracting variables.
Decellularization was performed via the three-day protocol. The adipose tissues were subjected to chemical decellularization with enzymatic solutions and deionized water. The tissues were submerged into a 1:1 solution of 0.05% Trypsin-EDTA and 0.032 M deoxycholic acid (Sigma-Aldrich, St. Louis, MO, USA). The adipose tissues were then thoroughly submerged in a 1:1 solution of 0.02% Trypsin and deoxycholic acid at 20°C and incubated overnight for 48 hours. This enzymatic digestive solution dissociates protein and adherent cells. The amount of solution used was five times the tissue mass. Subsequently, the tissues were rinsed with 30 ml deionized water. Temperature and pH (approximately pH 7) were measured to determine whether other accidental chemical reactions occurred. Following a washing course in deionized water, the tissues were transferred into the solutions containing Triton X-100 (Sigma-Aldrich) and deionized water for six hours. The tissue was then put in deionized water to re-rinse for six hours. Finally, the adipose segments were mechanically compressed for dehydration and then stored at 4°C.
To investigate the DNA concentration after treatment, Pico-green dsDNA assay (Invitrogen, Camarillo, CA, USA) was performed [33]. Since it is a colorimetric procedure, the test materials for analysis must be free from particulate materials such as cell debris and insoluble ECM fragments. To expose DNA contents, acid–pepsin digestion was applied to the tissues. They were submerged in 0.1 mg pepsin/ml 0.5 M acetic acid, which works as an enzyme for eliminating the terminal non-helical telopeptides to release the ingredients into solution. After pre-experiment to prepare samples for evaluation, DNA concentration was measured by VERSA Max Tunable Microplate Reader (Molecular Devices Corp., San Jose, CA, USA).
The amount of remaining collagen after treatment was evaluated by assaying soluble collagen with a sircol collagen assay (SCA) kit (Biocolor Ltd., County Antrim, UK). Briefly, SCA is a colorimetric procedure therefore tissue were freed of cell debris and insoluble ECM fragments. The test samples (10 mg each) were homogenized in acetic acid with pepsin. Each sample was incubated at 4°C and separated into pellet and supernatant by centrifugation. Sircol dye reagent that binds to collagen was applied to each sample. After centrifugation, an alkaline reagent was added to the pellet. The absorbance was measured at 540 nm wavelength on a microplate reader.
A non-toxic, cost-effective, and short DE-ECM processing methodology including supercritical extraction and enzymatic decellularization was established. Adipose tissues were treated with different process protocols (pre-enzyme or pre-supercritical process). After the completed processes, the white colored matrix with significantly decreased mass was collected (Fig. 3). Macroscopically, the raw adipose tissue size was different according to its thickness because of mechanical compression, but the produced DE-ECM had a similar appearance with it being whiter than the raw tissue after the entire processes.
The yield rate of DE-ECM with different extracting parameters was compared (Table 2). Adipose tissues with three different thicknesses were processed via the pre-enzyme or pre-supercritical process at three different pressures and two different temperatures. The tissue weight before and after processing was measured. It was found that yield rate depends on the extracting temperature and pressure. Fig. 4 shows the influence of extracting pressure and temperature on yield rate. The yield rates at 40°C±5°C using different protocols and at different pressures were as follows: pre-enzyme process at 1.01×107 Pa: 25.13%±4.02%, 2.03×107 Pa: 40.87%±3.09%, and 3.04×107 Pa: 45.62%±3.75%; pre-supercritical process at 1.01×107 Pa: 14.40%±3.54%, 2.03×107 Pa: 19.31%±5.95%, and 3.04×107 Pa: 21.47%±5.58%. Similarly, the yield rates at 30°C±5°C were: pre-enzyme process at 1.01×107 Pa: 18.34%±7.46%, 2.03×107 Pa: 26.58%±4.35%, and 3.04×107 Pa: 34.04%±4.04%; pre-supercritical process at 1.01×107 Pa: 4.85%±3.04%, 2.03×107 Pa: 15.49%±2.47%, and 3.04×107 Pa: 21.74%±8.12%. Yield rate increased when high temperature or pressure was applied. Furthermore, pre-enzyme treatment had higher processed DE-ECM yield rate percent than that of pre-supercritical treatment. The maximum yield rate observed was nearly 46% at 3.04×107 Pa pressure and 40°C±5°C temperature using the pre-enzyme process.
Table 2 . Extraction yield of decellularized extracellular matrix product with different extraction condition.
Adipose tissue | Process | Pressure (×107 Pa) | Temperature (±5°C) | Weight of original mass (g) | Weight of product (g) |
---|---|---|---|---|---|
1 | PE | 1.01 | 30 | 0.21 | 0.17 |
40 | 0.20 | 0.16 | |||
2.03 | 30 | 0.22 | 0.15 | ||
40 | 0.25 | 0.15 | |||
3.04 | 30 | 0.23 | 0.15 | ||
40 | 0.20 | 0.09 | |||
PS | 1.01 | 30 | 0.15 | 0.15 | |
40 | 0.24 | 0.20 | |||
2.03 | 30 | 0.24 | 0.19 | ||
40 | 0.19 | 0.14 | |||
3.04 | 30 | 0.20 | 0.14 | ||
40 | 0.17 | 0.12 | |||
2 | PE | 1.01 | 30 | 0.47 | 0.37 |
40 | 0.45 | 0.34 | |||
2.03 | 30 | 0.61 | 0.47 | ||
40 | 0.49 | 0.29 | |||
3.04 | 30 | 0.52 | 0.33 | ||
40 | 0.64 | 0.38 | |||
PS | 1.01 | 30 | 0.44 | 0.35 | |
40 | 0.43 | 0.38 | |||
2.03 | 30 | 0.46 | 0.39 | ||
40 | 0.53 | 0.46 | |||
3.04 | 30 | 0.45 | 0.36 | ||
40 | 0.42 | 0.35 | |||
3 | PE | 1.01 | 30 | 0.62 | 0.56 |
40 | 0.62 | 0.44 | |||
2.03 | 30 | 0.60 | 0.42 | ||
40 | 0.62 | 0.35 | |||
3.04 | 30 | 0.70 | 0.48 | ||
40 | 0.60 | 0.35 | |||
PS | 1.01 | 30 | 0.67 | 0.64 | |
40 | 0.70 | 0.60 | |||
2.03 | 30 | 0.89 | 0.80 | ||
40 | 0.62 | 0.51 | |||
3.04 | 30 | 0.78 | 0.66 | ||
40 | 0.67 | 0.55 |
Adipose tissue 1: thickness 1.9×10-3 m, Adipose tissue 2: thickness 5.7×10-3 m, Adipose tissue 3: thickness 9.5×10-3 m..
PE, pre-enzyme process; PS, pre-supercritical process..
The DNA content in DE-ECM tissues was compared with that of native adipose tissue (measured average DNA concentration: 0.065 µg/ml). Fig. 5 shows the concentration of remaining DNA after decellularization and supercritical extraction at different temperatures and pressures (DNA concentration of DE-ECM tissues produced using pre-enzyme process at 40°C±5°C—1.01×107 Pa: 49.23%±3.48%, 2.03×107 Pa: 24.62%±4.35%, and 3.04×107 Pa: 10.77%±3.43%; DNA concentration of DE-ECM tissues using produced pre-supercritical process at 40°C±5°C—1.01×107 Pa: 61.54%±1.10%, 2.03×107 Pa: 56.92%±2.39%, and 3.04×107 Pa: 27.69%±1.31%; DNA concentration of DE-ECM tissues produced using pre-enzyme process at 30°C±5°C—1.01×107 Pa: 24.62%±5.52%, 2.03×107 Pa: 18.46%±3.36%, and 3.04×107 Pa: 9.23%±0.38%; DNA concentration of DE-ECM tissues using produced pre-supercritical process at 30°C±5°C—1.01×107 Pa: 38.46%±6.16%, 2.03×107 Pa: 30.77%±10.22%, and 3.04×107 Pa: 21.54%±3.18%). DNA concentration of DE-ECM tissues extracted using pre-enzyme process at 3.04×107 Pa and 30°C±5°C was the lowest, with nearly 90% DNA being removed. This result indicates that the different kinds of ingredients, which contain different value of DNA contents, are extracted because of solubility difference.
The influence of temperature and pressure on the collagen concentration is presented in Fig. 6. The collagen amount in DE-ECM tissues were compared to those in original native adipose tissue (measured collagen content: ~0.90±0.03 µg/ml). Fig. 6 indicates that collagen amount steadily decreased with increase in extracting pressure from 1.01×107 to 3.04×107 Pa. Moreover, DE-ECM tissues produced at 20°C±5°C had more collagen than the tissues processed at 30°C±5°C and 40°C±5°C. At 40°C±5°C, the collagen content of DE-ECM were 24.88%±2.44%, 14.08%±2.10%, and 8.11%±6.87% at 1.01×107 Pa, 2.03×107 Pa, and 3.04×107 Pa, respectively. At 30°C±5°C, they were 33.97%±0.67%, 22.59%±0.79%, and 17.72%±4.86% at 1.01×107, 2.03×107, and 3.04×107 Pa, respectively. Similarly, at 20°C±5°C, they were 75.74%±1.83%, 43.17%±3.57%, and 32.11%±4.78% at 1.01×107 Pa, 2.03×107 Pa, and 3.04×107 Pa, respectively.
The purpose of this study was to produce biocompatible DE-ECM by a cost-effective, short, and non-toxic process. Supercritical fluid extraction with carbon dioxide (SC-CO2) and decellularization with enzymatic solutions were applied to treat DE-ECM. The combination of SC-CO2 and enzyme treatment produced DE-ECM samples in 70 hours cost-effectively and satisfactorily eliminated DNA. To increase solvent solubility, different experiment parameters such as extracting pressure and temperature were investigated by increasing the solvent density [34,35]. However, in a different aspect, temperature had a severe effect on the collagen composition of DE-ECM since collagen is vulnerable at high temperature [36,37]. DNA analysis showed that extraction using pre-enzyme process at 30°C±5°C and 3.04×107 Pa was the optimal condition to decrease DNA concentration, that is, DNA concentration decreased from 0.065 µg/ml of original adipose tissue to 0.006 µg/ml of produced DE-ECM. Collagen is a critical element in pharmaceutical and biomedical industries and has an important role in tissue and organ formation due to ultimate biocompatibility with the immune system. The collagen analysis result shows that DE-ECM produced at optimal extraction conditions using the pre-enzyme process had 0.16 µg/ml collagen; 17.72%. Thus, high pressure and low temperature are the effective variables to produce biocompatible DE-ECM. Application of supercritical fluid extraction and enzyme decellularization process proves that cost-effective, non-toxic, and less time-consuming production of medically available DE-ECM is possible without using any unnecessary chemicals that damages the biostructure. Moreover, controlling pressure and temperature provides optimal biocompatibility and has a potential usage of supercritical fluid extraction in DE-ECM mass production, as it is a rapid process. This study evaluated the feasibility of utilizing supercritical extraction technology in biomaterials and it was proven successful. Moreover, medically available DE-ECM can be utilized in tissue regeneration therapeutics including medical pad with drugs as well as new drug delivery paradigm.
The authors have nothing to disclose.
Table 1 . Summary of decellularization agents and technique for producing decellularized extracellular matrix tissue.
Agent/technique | Mechanism | Effect | Reference |
---|---|---|---|
Acids and base | Solubilize cytoplasmic components of cells and tend to denature proteins. | Decrease collagen amount and GAG. | [15,16] |
Hypotonic and hypertonic | Occur Cell lysis by osmotic shock and disrupt DNA-protein interactions. | Non-effective in removing cellular residue. | [17] |
Tributyl phosphate | Form stable complexes with metals and disrupt protein-protein interactions. | Mixed results with efficacy dependent on tissue, dense tissues lost collagen. | [18] |
Nucleases | Catalyze the hydrolysis of ribonucleotide. | Difficult to remove from the tissue and invoke an immune response. | [19] |
Freezing | Intracellular ice crystals disrupt cell membrane. | Ice crystal formation disrupts or fracture in product. | [20] |
Electroporation | Pulsed electrical fields disrupt cell membranes. | Electrical field oscillation disrupts ECM structure. | [21] |
Agitation | Lyse cells and facilitate chemical exposure. | Aggressive agitation or sonication damages ECM. | [21] |
Perfusion | Facilitate chemical exposure and removal of cellular material. | Pressure associated with perfusion disrupt ECM. | [22] |
GAG, glycosaminoglycans; ECM, extracellular matrix..
Table 2 . Extraction yield of decellularized extracellular matrix product with different extraction condition.
Adipose tissue | Process | Pressure (×107 Pa) | Temperature (±5°C) | Weight of original mass (g) | Weight of product (g) |
---|---|---|---|---|---|
1 | PE | 1.01 | 30 | 0.21 | 0.17 |
40 | 0.20 | 0.16 | |||
2.03 | 30 | 0.22 | 0.15 | ||
40 | 0.25 | 0.15 | |||
3.04 | 30 | 0.23 | 0.15 | ||
40 | 0.20 | 0.09 | |||
PS | 1.01 | 30 | 0.15 | 0.15 | |
40 | 0.24 | 0.20 | |||
2.03 | 30 | 0.24 | 0.19 | ||
40 | 0.19 | 0.14 | |||
3.04 | 30 | 0.20 | 0.14 | ||
40 | 0.17 | 0.12 | |||
2 | PE | 1.01 | 30 | 0.47 | 0.37 |
40 | 0.45 | 0.34 | |||
2.03 | 30 | 0.61 | 0.47 | ||
40 | 0.49 | 0.29 | |||
3.04 | 30 | 0.52 | 0.33 | ||
40 | 0.64 | 0.38 | |||
PS | 1.01 | 30 | 0.44 | 0.35 | |
40 | 0.43 | 0.38 | |||
2.03 | 30 | 0.46 | 0.39 | ||
40 | 0.53 | 0.46 | |||
3.04 | 30 | 0.45 | 0.36 | ||
40 | 0.42 | 0.35 | |||
3 | PE | 1.01 | 30 | 0.62 | 0.56 |
40 | 0.62 | 0.44 | |||
2.03 | 30 | 0.60 | 0.42 | ||
40 | 0.62 | 0.35 | |||
3.04 | 30 | 0.70 | 0.48 | ||
40 | 0.60 | 0.35 | |||
PS | 1.01 | 30 | 0.67 | 0.64 | |
40 | 0.70 | 0.60 | |||
2.03 | 30 | 0.89 | 0.80 | ||
40 | 0.62 | 0.51 | |||
3.04 | 30 | 0.78 | 0.66 | ||
40 | 0.67 | 0.55 |
Adipose tissue 1: thickness 1.9×10-3 m, Adipose tissue 2: thickness 5.7×10-3 m, Adipose tissue 3: thickness 9.5×10-3 m..
PE, pre-enzyme process; PS, pre-supercritical process..