Optimal processing conditions of Boswellia carteri Birdw. using response surface methodology
Jee-Hyun Yoon1, Jung-Hoon Kim2, Seong-Sik Ham1, Bu-Yeon Gang1, Seung-Ho Lee3, Goya Choi4, Young-Sik Kim5, Guemsan Lee6, Young-Sung Ju1
1 Department of Herbology, College of Korean Medicine, Woosuk University, Jeonju-si, Jeollabuk-do 54986, Republic of Korea
2 Division of Pharmacology, School of Korean Medicine, Pusan National University, Yangsan-si, Gyeongsangnam-do 50612, Republic of Korea
3 Mibyeong Research Center, Korea Institute of Oriental Medicine, Yuseong-gu, Daejeon 34054, Republic of Korea
4 K–Herb Research Center, Korea Institute of Oriental Medicine, Yuseong-gu, Daejeon 34054, Republic of Korea
5 Department of Herbal Pharmacology, College of Korean Medicine, Kyung Hee University, Dongdaemun-gu, Seoul 02447, Republic of Korea
6 Department of Herbology, College of Korean Medicine, Wonkwang University, Iksan-si, Jeollabuk-do 54538, Republic of Korea
|Date of Submission||11-Apr-2017|
|Date of Acceptance||25-Apr-2017|
|Date of Web Publication||10-Apr-2018|
Department of Herbology, College of Korean Medicine, Woosuk University, 61, Seonneomeo 3-gil, Wansan-gu, Jeonju-si, Jeollabuk-do 54986
Republic of Korea
Source of Support: None, Conflict of Interest: None
| Abstract|| |
Background: Boswellia carteri Bridw. is being widely used for its anti-inflammatory properties, as well as for wound healing, antimicrobial, and immunomodulatory properties, and boswellic acids (BAs) are considered to be the main active constituents. Objectives: To investigate optimal conditions of stir-baking process for the resin of B. carteri with vinegar of using response surface methodology (RSM). Materials and Methods: The concentration of acetic acid, heating temperature, and heating time were set as influential factors, and the yields of chemical compounds were the response values which were optimally designed by a Box–Behnken design. The amounts of 11-keto-β-boswellic acid (KBA) and α-boswellic acid (αBA) in B. carteri resin were quantified using high-performance liquid chromatography analysis. Results: Maximum amounts of KBA and αBA in B. carteri resin were obtained using 6% acetic acid for 10 min at 90°C in preliminary test. Two factor interactions, such as acetic acid concentration–heating temperature and heating temperature–heating time, were significantly observed by multiple regression analysis. Optimal processing conditions from RSM were 5.83% for acetic acid concentration, 9.56 min for heating time, and 89.87°C for heating temperature. Under the modified conditions, the experimental value of the response was 11.25 mg/g, which was similar to the predicted value. Conclusions: The results suggest that the optimal conditions for the stir-baking process of B. carteri resin were determined by RSM, which was reliable and applicable to practical processing of herbal medicine.
Abbreviations used: BAs: Boswellic acids; KBA: 11 keto β boswellic acid; αBA: α boswellic acid; BBD: Box–Behnken design; RSM: Response surface method; HPLC: High performance liquid chromatography; LOD: Limits of determination; LOQ: Limits of quantification; RSD: Relative standard deviation; ANOVA: Analysis of variance.
Keywords: Boswellia carteri, high-performance liquid chromatography, optimization, processing conditions, response surface methodology
|How to cite this article:|
Yoon JH, Kim JH, Ham SS, Gang BY, Lee SH, Choi G, Kim YS, Lee G, Ju YS. Optimal processing conditions of Boswellia carteri Birdw. using response surface methodology. Phcog Mag 2018;14:235-41
|How to cite this URL:|
Yoon JH, Kim JH, Ham SS, Gang BY, Lee SH, Choi G, Kim YS, Lee G, Ju YS. Optimal processing conditions of Boswellia carteri Birdw. using response surface methodology. Phcog Mag [serial online] 2018 [cited 2021 Sep 20];14:235-41. Available from: http://www.phcog.com/text.asp?2018/14/54/235/229677
- The resin of Boswellia carteri was macerated in aqueous acetic acid and heated using an oven for stir baking process
- The interaction between heating temperature and heating time was the most significant
- Optimal conditions for processing B. carteri resin were determined as 5.83% acetic acid, 9.56 min for heating time, and 89.87°C for heating temperature.
| Introduction|| |
Olibanum is an oleogum resin produced by Boswellia carteri Birdw. and other Boswellia genus. Its medicinal properties lie in the treatment of pain in the epigastrium, various kinds of injuries, and bruises. It is also used for blood stasis syndrome in gynecology diseases, such as dysmenorrhea. The resin of B. carteri is a complex mixture composed of essential oils (mono- and sesquiterpenes), alcohol-soluble resins (di- and triterpenes), and water-soluble gums. Especially, the triterpenes, α-boswellic acid (αBA) and β-boswellic acids (βBA) and their derivatives, constitute the main pharmaceutical activity., These compounds in B. carteri resin show anti-inflammatory effects because of the inhibitory activity on 5-lipoxygenase by the boswellic acids (BAs).,, Recently, incensole acetate and its derivatives were reported to be responsible for its anti-inflammatory effects. Furthermore, the BAs show immunomodulatory, cytotoxic, and anticancer activity.,,
Although some herbal medicines gathered from their habitats are used in natural form or after only drying, most of them need to undergo processing before use. Only after that the herbal medicines can present curative effects adequately and be used safely. Stir-baking, a fire-processing method, is used primarily to process olibanum with vinegar, as an assistant liquid material. In conventional processing, the herbal medicine is blended with brewed vinegar evenly at the ratio of 10:1 or 10:1.5. In sequence, olibanum is parched until its surface becomes glossy and then cooled. The purpose of processing olibanum as mentioned in numerous ancient texts is to remove impurities such as the tree barks and grains of sand, and to facilitate decoction, the preparation can be easily crushed because of its viscosity., By this method, the smell and taste of drugs can be altered to facilitate their administration. Moreover, vinegar-baked olibanum has the enhanced therapeutic effects of relieving pains and promoting the circulation of blood.
A previous study reported a comparison of the concentration of acetyl-11-keto-β-boswellic acid (%) between olibanum and processed olibanum, but the result was not statistically significant. Even though B. carteri resin extract showed the pharmacological effectiveness against inflammatory diseases in many studies,, there has been insufficient scientific evaluation of the changes in the chemical composition during processing, which is essential for its effective and safe usage.
The aims of this study were to establish the analytical methods of marker compounds in the methanol extract of B. carteri resin and to find optimal processing conditions of B. carteri resin with vinegar, adjusting several variables such as acetic acid concentration, heating temperature, and heating time using a Box–Behnken design (BBD) with a response surface method (RSM) for statistical analysis.
| Materials and Methods|| |
Material and reagents
The crude drugs of B. carteri were purchased from Kwangmyungdang Medicinal Herbs (Ulsan, Korea) and authenticated by Prof. Ju (Department of Herbology, Woosuk University, Republic of Korea). A voucher specimen (2014-WS-BC) has been deposited in the Department of Herbology of Woosuk University.
Two marker compounds, 11-keto-β-boswellic acid (KBA) and αBA, with the purity of both compounds >95%, were obtained from Fluka (Buchs, Switzerland). Their chemical structures are shown in [Figure 1]. High-performance liquid chromatography (HPLC) grade acetonitrile and water were purchased from J.T. Baker Inc. (Phillipsburg, NJ, USA), and HPLC grade methanol was purchased from Merck Chemical Co. (Darmstadt, Germany). Acetic acid was obtained from Fluka (Buchs, Switzerland).
|Figure 1: Chemical structures of the two marker compounds in the methanol extract of Boswellia carteri resin. 1, 11-keto-β-boswellic acid; 2, α-boswellic acid|
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Standardized procedure of stir-baking with acetic acid
The resin of B. carteri was macerated for 10 min in aqueous acetic acid, and then, samples were dried at room temperature for 24 h. The dried resins were heated using a vacuum oven (OV-12, Jeio Tech Co., Daejeon, Korea), while adjusting factors such as heating temperature and heating time. To find the optimal conditions for processing of B. carteri resin, preliminary single-factor tests were performed to determine the required range of acetic acid concentration (X 1, 3%–12%), heating temperature (X 2, 60°C–150°C), and heating time (X 3, 5–20 min).
Sample extraction for high-performance liquid chromatography analysis
The processed resins were powdered and a 200 mg of powdered resin was extracted with 2 mL methanol using ultrasonication for 50 min at 50°C. The methanol extract was centrifuged at 10,000 rpm for 20 min. The supernatants were concentrated in vacuo to dryness at 45°C for 24 h. The concentrated extract was dissolved in methanol at the concentration of 10 mg/mL and filtered through a 0.20 μm syringe filter before injecting into the HPLC.
High-performance liquid chromatography analytical conditions
The methanol extracts of B. carteri resin were analyzed using an Agilent 1200 (Agilent Technologies, Palo Alto, CA, USA) equipped with an autosampler, degasser, quaternary solvent pump, and diode array detector. Separation was performed on an Eclipse XDB C8 column (150 mm × 4.6 mm, 5 μm; Agilent) at 35°C. The mobile phase consisted of 0.1% trifluoroacetic acid in water (TFA; A) and acetonitrile (B). The following gradient (B%) was applied to the elution of marker compounds: 75%–75% (B) over 0–2 min, 75%–88% (B) over 2–12 min, held for 3 min, and then re-equilibrated to 75% until the end of analysis. The flow rate was set to 1.0 mL/min and the detection wavelength was determined at 250 nm for KBA and 280 nm for αBA.
Linearity, limit of detection, and limit of quantification
The stock solutions were prepared in methanol by dissolving accurately weighed standard compounds at concentrations of 1000 μg/mL. Working solutions produced by diluting the stock solutions were used to construct calibration curves. The diluted concentrations of marker compounds were plotted against the peak areas and calibration curves were used to evaluate the linearity.
The blank samples were injected three times and the area of the noise peak was calculated. Limit of detection (LOD) and limit of quantification (LOQ) were determined as follows: LOD = 3.3 × standard deviation (SD)/slope of regression; LOQ = 10 × SD/slope of regression.
Precision, recovery, and reproducibility
The precision was evaluated for intra-day (n = 3) and inter-day (n = 3) by analyzing standard mixture solutions containing low and high concentrations of marker compounds. The values were calculated as the relative SD: RSD (%) = (SD/mean) × 100.
A recovery test was evaluated to determine the accuracy of the method. Experiments were carried out by adding two known amounts of marker compounds (low and high) to samples. The recovery was represented as follows: Recovery (%) = ([detected concentration − initial concentration)/spiked concentration) × 100.
The reproducibility was evaluated by calculating the RSD values for the retention times and the absolute areas of marker compounds (n = 5).
Experimental design and statistical analysis
A three-level-three-factor BBD was employed to determine the optimal processing conditions for B. carteri resin, with quantification of the two marker compounds.
Obtained experimental data from the BBD were fitted to a second-order polynomial model and the regression coefficients were calculated using the equation:
where Y is the estimated response, β 0, β j, β jj, and β ij are the regression coefficients for intercept, linearity, square, and interaction terms, respectively. Xi and Xj are the independent variables, which were coded as −1, 0, and 1.
The fitness of the second-order polynomial model was investigated through the term of lack-of-fit and coefficient of determination (r2). F and Pvalues were calculated using an ANOVA test and the significance of the regression coefficients determined at P < 0.05 or 0.01 was evaluated. Three-dimensional (3-D) response surface plots and contour plots were used to represent the interaction and influence of the three variables on the yield of the two marker compounds. The open-source software R (version 3.1.1; The R Foundation for Statistical Computing) was employed to generate the experimental design, perform statistical analysis, and evaluate the regression model.
| Results|| |
Under the developed HPLC methods developed above, the two marker compounds showed apparent separation and any interference was not found on the chromatograms at their maximum absorption wavelengths [Figure 2]. Capacity factor (k), relative retention (α), resolution (Rs), theoretical plate number (N), and symmetry (S) were evaluated using the peaks of the two marker compounds. The range of the capacity factor was 2 < k<7, the relative retention was 2< α<3, the resolution was >40, the theoretical plate number was 30,000< N <70,000, and symmetry was 0.9< S <1.1, which indicate that the two marker peaks were separated, and tailing or peak fronting was not observed [Table 1].
|Figure 2: Chromatograms of a standard mixture (a) and methanol extracts of Boswellia carteri resin (b and c). 1, 11-keto-β-boswellic acid; 2, α-boswellic acid|
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Linear regression, limit of detection, and limit of quantification
The linearity, which was represented as the correlation coefficient (r2) of KBA and αBA, was 0.9999 and 0.9998, respectively. The values of the LODs and LOQs of the two compounds were 0.24 and 0.46 μg/mL and 0.74 and 1.38 μg/mL, respectively [Table 2].
|Table 2: Linear equations, coefficients of determination (r2), limit of detection, and limit of quantification for the bioactive compounds|
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Precision, recovery, and reproducibility
The intra-day and inter-day precision of the two marker compounds was calculated as RSD values and their values were ≤2.0% in two concentration levels [Table 3]. The recoveries of the two compounds were 95.36%–105.98%, with RSD values of <3.0% [Table 4]. The reproducibility of the two marker compounds was also calculated as RSD values and their values were <0.1% for the retention time and <2.0% for the absolute area (n = 5).
Regression analysis and model fitting
The required ranges of acetic acid concentration (X 1, 3%–9%), heating temperature (X 2, 60°C–120°C), and heating time (X 3, 5–15 min) were determined for BBD from the results of preliminary single-factor tests [Figure 3].
|Figure 3: The results of a preliminary test within the selected ranges of independent variables. (a) Concentration of acetic acid. (b) Heating temperature. (c) Heating time|
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The regression coefficients of the predicted quadratic polynomial model were calculated by the coded values and responses from the BBD of the experiment and the significance of each coefficient was determined by the Pvalue. A significant interaction between two variables was observed: the concentration of acetic acid (X 1) and heating temperature (X 2) (P < 0.05); and heating temperature (X 2) and heating time (X 3) (P < 0.001). However, the linear terms (X 1, X 2, X 3), quadratic terms (X 1:X 1, X 2:X 2, X 3:X 3), and two-factor interaction (X 1:X 3) were not significantly influential on the regression model (P > 0.05) [Table 5].
|Table 5: Regression coefficients of the predicted quadratic polynomial model|
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The regression coefficient of the model was applied to determine the predicted response values and was calculated by the following second-order polynomial equation: Y (response) = 11.930379 + 0.042851X1 +0.188227X2 +0.027972X3 +0.460208X1 X2 +0.289783X1 X3 +1.840442X2 X3 +0.134214X1 X1 − 0.022731X2 X2 +0.020012X3 X3, where Y is the yield of the two compounds (mg/g) and the coded variables, X 1, X 2, and X 3, represent the concentration of acetic acid, heating temperature, and heating time, respectively.
An ANOVA was performed for the fitted quadratic polynomial model for the yield of the two compounds, showing that two-factor interaction was significant with F > 49 and P < 0.001, respectively [Table 6]. The coefficients of determination for multiple R2 and adjusted R2 were 0.9618 and 0.9045, respectively, with a significant lack-of-fit at P < 0.05.
|Table 6: Analysis of variance for the fitted quadratic polynomial model for the extraction of compounds|
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Analysis of response surface
The interaction between variables and their influences on the response, the yields of the two marker compounds, was graphically visualized via a 3-D response plots and two-dimensional (2-D) contour plots, where the response values from the BBD obtained from regression analysis above were applied.
The predicted values of response were calculated by the second-order polynomial equation above using the coded values of X 1, X 2, and X 3, respectively [Table 7]. The coded values at two margins, 1.0:−1.0 and −1.0:1.0, produced less yield of the two marker compounds compared with those at the margins of −1.0: −1.0 and 1.0:1.0 in all 3-D surface plots and 2-D contour plots and the response surface derived from each margin formed curves, which was most apparent in the plot of X 2:X 3 interaction at the zero level of X 1 [Figure 4].
|Table 7: Experimental ranges and values of the independent variable in the Box-Behnken design for processing conditions|
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|Figure 4: Response surface plots and contour plots of the interactions between acetic acid concentration (χ1, %), temperature (χ2, °C), and time (χ3, min)|
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Optimization and verification of the stir-baking processing of Boswellia carteri resin by response surface methodology
The conditions that produced the optimal response of the stir-baking processing of B. carteri resin were determined as coded values: −0.05725 of X 1 (acetic acid concentration; %); −0.00427 of X 2 (heating temperature; °C); and − 0.08806 of X 3 (heating time; min). The optimized coded values were calculated to actual values, namely 5.83% of acetic acid concentration, 89.87°C of heating temperature, and 9.56 min of heating time, respectively, which produced 11.93 mg/g of predicted response, determined by the second-order polynomial equation above. The modified conditions represented 11.25 mg/g, which was very close to the actual response [Table 8]. These results confirm that the model for the stir-baking processing was able to predict the experimental conditions.
|Table 8: Optimum conditions and the predicted and experimental values of the response at the optimum conditions|
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| Discussion|| |
Optimization of chromatographic conditions
The mobile phase, modifier, and ultraviolet (UV) wavelength of the diode array detection were chosen to be crucial factors of HPLC analysis. A C8 column was selected to separate the peak of KBA from adjacent peaks because a C18 column was not able to separate overlapping peaks. The mobile phase consisting of water (solvent A) and acetonitrile (solvent B) was used for the analysis. Various modifiers, such as 0.5% acetic acid, 0.1% phosphoric acid, 0.1% TFA, and 0.1% formic acid, were tested to obtain distinct separation between the peaks of the two marker compounds and adjacent peaks. Resolution and peak shapes of the two marker compounds were achieved when using 0.1% TFA as a modifier. The UV wavelengths of maximum absorption were chosen to determine the optimal absorption wavelength for each marker compound, namely KBA for 250 nm and αBA for 280 nm, as previously reported.,,
Fitting of the regression model
To predict quadratic polynomial models for the stir-baking processing of B. carteri resin, multiple regression coefficients were calculated using least squares methodology. ANOVA represents the adequacy of the selected variables of polynomial models. The model coefficient of multiple R2 indicates that the predicted model could explain 96.18% of the results and only 3.82% of the total variance was not explained by the model; adjusted R2 also represents the same explanation as above, at a level of significance (P < 0.02). These results demonstrate that this multiple regression model is adequate and can explain most of the variability for variables because a larger t-value and smaller Pvalue show the significance of the corresponding coefficient.
In ANOVA, the parameter for two-factor interaction was highly significant for all variables (P < 0.001), while linear and quadratic parameters were not significant (P > 0.05). Hence, the interactions between variables were the primary determining terms that might affect significantly on the response with insignificant linear and quadratic terms. However, there is significant lack-of-fit in this model (P < 0.05). The nonsignificant value of lack-of-fit (P > 0.05) revealed that the quadratic model is statistically significant for the response, and therefore, it can be used for further analysis. Evidence of lack-of-fit may come from a violation of one or more of three characteristics: (1) the fitted model's residual variation is small; (2) displays no systematic tendency; and (3) follows the variability postulated by the model.
Box–Behnken design and response surface methodology
RSM has been used to determine the optimum conditions of independent variables that produce the maximum value of response, showing visual interaction of two independent variables via 3-D response plots and 2-D contour plots. BBD is a class of second-order designs based on three-level incomplete factorial designs, and because they do not contain combinations for which all factors are simultaneously at their highest or lowest levels, they are considered useful in avoiding experiments conducted under extreme conditions, for which undesirable results may occur. RSM combined with BBD has been successfully applied to optimizing the extraction conditions – such as extraction temperature, extraction time, or ratio of raw materials to solvents – of chemical compounds or polysaccharides from herbal medicines using various extraction methods.,,, A convex response plot and an elliptical contour plot usually indicate that the interaction between the variables is significant, while a circular contour plot means negligible interaction.
However, the response plots and contour plots in this study did not show typical convex and elliptical shapes; instead, they showed the curves focused in the middle values. These results indicate that the variables that produce the optimum value of response, not the maximum value, can be determined by the response and contour plots, because the response values from both contrary margins were gathered in one point. In the present study, the interaction between acetic acid concentration (%) and heating temperature (°C) showed weak influential interaction on the yield of the two marker compounds, at a level of significance (P < 0.05), while the heating temperature (°C) and heating time (min) strongly interacted and significantly affected the yield of the two marker compounds (P < 0.001). Therefore, the two factors of heating temperature and heating time are thought to be key factors in determining optimal stir-baking processing of the B. carteri resin with acetic acid.
Strengths and limitations of this study
In the present study, analytical conditions for the marker compounds in B. carteri resin extract were established with validated methods. Using statistical tools, optimized conditions for stir-baking processing of B. carteri resin with vinegar was performed, while adjusting three influential factors – acetic acid concentration, heating temperature, and heating time – with the aim of providing objective processing methods for the herbal medicine. However, two chemical marker compounds cannot guarantee the entire chemical characteristics and therapeutic effect of B. carteri resin. Moreover, there may be other influential variables, such as extraction solvent and time of maceration in aqueous acetic acid, and these should be considered in further study.
| Conclusions|| |
Established analytical methods were applied to quantify two marker compounds in a B. carteri resin extract. Two factor interactions – acetic acid concentration–heating temperature and heating temperature–heating time – were significant; of these, the interaction between heating temperature and heating time was the most significant. Optimal conditions for stir baking process of B. carteri resin were determined as 5.83% acetic acid, 89.87°C for heating temperature, and 9.56 min for heating time, which were modified to 6.00%, 90.00°C, and 10 min, respectively.
Financial support and sponsorship
This research was supported by the “2014 KIOM Undergraduate Research Program” and “A Study of Article List for the Korean Medicinal Materials (1)” (K18401) funded by Korea Institute of Oriental Medicine.
Conflicts of interest
There are no conflicts of interest.
| References|| |
Ju YS. Ungok Herbology. 2nd
ed. Jeonju: Woosuk Press; 2013. p. 278-9, 941-4.
Basar S, Koch A, König WA. A verticillane-type diterpene from Boswellia carteri
essential oil. Flavour Frag J 2001;16:315-8.
Hamm S, Bleton J, Connan J, Tchapla A. A chemical investigation by headspace SPME and GC-MS of volatile and semi-volatile terpenes in various olibanum samples. Phytochemistry 2005;66:1499-514.
Banno N, Akihisa T, Yasukawa K, Tokuda H, Tabata K, Nakamura Y, et al.
Anti-inflammatory activities of the triterpene acids from the resin of Boswellia carteri
. J Ethnopharmacol 2006;107:249-53.
Fan AY, Lao L, Zhang RX, Wang LB, Lee DY, Ma ZZ, et al.
Effects of an acetone extract of Boswellia carterii
) gum resin on rats with persistent inflammation. J Altern Complement Med 2005;11:323-31.
Safayhi H, Mack T, Sabieraj J, Anazodo MI, Subramanian LR, Ammon HP, et al.
Boswellic acids: Novel, specific, nonredox inhibitors of 5-lipoxygenase. J Pharmacol Exp Ther 1992;261:1143-6.
Moussaieff A, Mechoulam R. Boswellia
resin: From religious ceremonies to medical uses; A review of in-vitro
and clinical trials. J Pharm Pharmacol 2009;61:1281-93.
Badria FA, Mikhaeil BR, Maatooq GT, Amer MM. Immunomodulatory triterpenoids from the oleogum resin of Boswellia carterii
birdwood. Z Naturforsch C 2003;58:505-16.
Camarda L, Dayton T, Di Stefano V, Pitonzo R, Schillaci D. Chemical composition and antimicrobial activity of some oleogum resin essential oils from Boswellia
). Ann Chim 2007;97:837-44.
Prakash B, Mishra PK, Kedia A, Dubey NK. Antifungal, antiaflatoxin and antioxidant potential of chemically characterized Boswellia carteri
Birdw. Essential oil and its in vivo
practical applicability in preservation of Piper nigrum
L. fruits. LWT Food Sci Technol 2014;56:240-7.
Kyung Hee University. A research on basic items in common medicinal herbs (4): A study on process of medicinal herbs preparation for medicinal herbs. In: Korea Institute of Oriental Medicine Research Report. Daejon, Korea: Korea Institute of Oriental Medicine; 1998. p. 652-4.
Korea Food and Drug Administration. The Korean Herbal Pharmacopoeia. Seoul: Shinil Books; 2012. p. 7-282.
Sun L, Liu L, Jin H, Tian J, Lin R. Determination of frankincense and processed frankincense. Chinese Pharm Aff 2010;24:972-4.
Belsner K, Büchele B, Werz U, Syrovets T, Simmet T. Structural analysis of pentacyclic triterpenes from the gum resin of Boswellia serrata
by NMR spectroscopy. Magn Reson Chem 2003;41:115-22.
Frank A, Unger M. Analysis of frankincense from various Boswellia
species with inhibitory activity on human drug metabolising cytochrome P450 enzymes using liquid chromatography mass spectrometry after automated on-line extraction. J Chromatogr A 2006;1112:255-62.
Kim SH, Kim HK, Yang ES, Lee KY, Kim SD, Kim YC, et al
. Optimization of pressurized liquid extraction for spicatoside a in Liriope platyphylla
. Sep Purif Technol 2010;71:168-72.
Liyana-Pathirana C, Shahidi F. Optimization of extraction of phenolic compounds from wheat using response surface methodology. Food Chem 2005;93:47-56.
Sharma P, Singh L, Dilbaghi N. Optimization of process variables for decolorization of Disperse Yellow 211 by Bacillus subtilis
using Box-Behnken design. J Hazard Mater 2009;164:1024-9.
Hosmer DW, Hosmer T, Le Cessie S, Lemeshow S. A comparison of goodness-of-fit tests for the logistic regression model. Stat Med 1997;16:965-80.
Sun Y, Liu J, Kennedy JF. Application of response surface methodology for optimization of polysaccharides production parameters from the roots of Codonopsis pilosula
by a central composite design. Carbohydr Polym 2010;80:949-53.
Ferreira SL, Bruns RE, Ferreira HS, Matos GD, David JM, Brandão GC, et al.
Box-Behnken design: An alternative for the optimization of analytical methods. Anal Chim Acta 2007;597:179-86.
Ye CL, Huang Q. Extraction of polysaccharides from herbal Scutellaria barbata
D. Don (Ban-Zhi-Lian) and their antioxidant activity. Carbohydr Polym 2012;89:1131-7.
Li W, Wang Z, Sun YS, Chen L, Han LK, Zheng YN, et al.
Application of response surface methodology to optimise ultrasonic-assisted extraction of four chromones in Radix Saposhnikoviae
. Phytochem Anal 2011;22:313-21.
Zhang J, Jia S, Liu Y, Wu S, Ran J. Optimization of enzyme-assisted extraction of the Lycium barbarum
polysaccharides using response surface methodology. Carbohydr Polym 2011;86:1089-92.
Li W, Zhao LC, Sun YS, Lei FJ, Wang Z, Gui XB, et al.
Optimization of pressurized liquid extraction of three major acetophenones from Cynanchumbungei
using a box-behnken design. Int J Mol Sci 2012;13:14533-44.
Muralidhar RV, Chirumamila RR, Marchant R, Nigam P. A response surface approach for the comparison of lipase production by Canida cylindracea
using two different carbon sources. Biochem Eng J 2001;9:17-23.
[Figure 1], [Figure 2], [Figure 3], [Figure 4]
[Table 1], [Table 2], [Table 3], [Table 4], [Table 5], [Table 6], [Table 7], [Table 8]