2020. 3. 2. 17:30ㆍ카테고리 없음
- Central Composite Design Minitab
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BackgroundHaemophilus influenzae type b (Hib) is the leading cause of bacterial meningitis, otitis media, pneumonia, cellulitis, bacteremia, and septic arthritis in infants and young children. The Hib capsule contains the major virulence factor, and is composed of polyribosyl ribitol phosphate (PRP) that can induce immune system response. Vaccines consisting of Hib capsular polysaccharide (PRP) conjugated to a carrier protein are effective in the prevention of the infections. However, due to costly processes in PRP production, these vaccines are too expensive. BackgroundBefore discovery of an effective vaccine, Haemophilus influenzae type b (Hib) was the most important cause of bacterial meningitis, otitis media, pneumonia, cellulitis, bacteremia, and septic arthritis in infants and children younger than five years (, ).
It is a significant public health concern in many parts of the world, with as many as 3 million cases of serious disease occurring every year. The Hib capsule is its major virulence factor, and is composed of a polyribosyl ribitol phosphate (PRP) that can induce protective and effective immunity. Hib PRP is a polymer of repeating monomeric units, structurally characterized as β-D-ribose-D-ribitol-phosphate (, ).
The first generation of vaccines for Hib was licensed in the United States in 1985, based on purified capsular polysaccharide. This type of vaccine stimulates a T cell-independent immune response and prevents Hib infections in children older than 2 years, but it does not protect infants.
Since about 75% of Hib infection cases occur in children younger than 2 years, second-generation Hib vaccines, which induced T-cell dependent immune responses, were produced as PRP-protein conjugates and licensed in the United States in 1987.The price of the conjugated PRP vaccine is high , and therefore a major challenge in Hib vaccine production is to develop a cost-efficient vaccine. To enhance biomass and PRP productions, most previous studies have focused on Hib cultivation with respect to essential chemical, biochemical, and physical factors such as pH, DOT (dissolved oxygen tension), aeration, temperature, and agitation (-). Most of these studies employed single factors or multiple factors by changing one variable at a time, while keeping the others at a constant level.
However, such growth conditions do not mimic the natural bacterial growth condition, which is affected by simultaneous actions and interaction of the growth factors. ObjectivesTherefore, in the present study, we used a central composite design (CCD) and a response surface methodology (RSM) to examine the main and/or interactive effects of a factorial combination of pH, temperature, and agitation treatment factors on the growth of Hib and biomass production. Response surface methodology enabled the identification of optimum levels of growth factors in maximizing Hib biomass, and more PRP production as a direct result (, ).
Response surface methodology guides the plan of the experiments and the parsimonious analysis of data to gain a maximum amount of information most efficiently (, ). Culture MediumThe culture medium was prepared according to the method explained by Maitre-Wilmotte et al. , with some modifications.
It had 5 mg of β-NAD (Sigma, Germany), 0.015 g of protoporphyrin IX (Sigma, Germany), 20 g of glucose (Merck, Germany), 5 g of dialyzed yeast extract (Sigma, Germany), 70 mg of cysteine (Sigma, Germany), 10 g of bactopepton (Difco, USA), 20 mg of tryptophan (Sigma, Germany), 31.14 g of Na 2HPO 4.12H 2O (Sigma, Germany), 2.03 g of NaH2PO4.2H2O (Sigma, Germany), 1 g of (NH4)2SO4 (Sigma, Germany), 0.4 g of MgSO 4.7H 2O (Sigma, Germany), and 0.02 g of CaCl 2.2H 2O (Sigma, Germany). All material was dissolved in de-ionized water to a final volume of 1 L, and the medium was filtered in a 0.8 µm (Millipore, Canada) membrane. Fifty mL of the culture medium was distributed to a non-baffled 250 mL Erlenmeyer and autoclaved at 121° C for 30 minutes.
Protoporphyrin was dissolved in 100 mM NaOH. Glucose, NAD, and protoporphyrin were sterilized separately by filtration with 0.22 µm (Millipore, Canada) membranes, and transferred to experimental flasks. Inoculation and Incubation ProcedureThe preparation of the working seed and inoculation of experimental culture flasks were done according to the methods explained by Merritt et al. A deep frozen 1 mL vial of Hib in 15% glycerol was thawed and transferred to two chocolate agar-slant tubes, then incubated at 37° C for 18 hours. The surface grown bacteria were harvested and re-suspended in 2 mL of the culture medium, and transferred to a 500 mL Erlenmeyer with 200 mL fresh culture medium. It was then incubated at 300 rpm in a shaker incubator at 37° C, for 6 - 8 hours.
5 mL of this culture was used to inoculate 45 mL of the culture medium in each of 250 mL experimental flasks. The temperature, agitation, and pH of each experimental flask were adjusted to the designed point. The flasks were grown for 19 hours. Dry Biomass DeterminationThe amount of dry cell weight (DCW) was determined by dry-weight measurement. After the cultivation period, each cultured medium was heat-deactivated at 60° C for 30 minutes and centrifuged at 3200 g, at 4° C for 60 minutes in pre-weighed tubes. The supernatant was saved for a PRP assay in the next steps, and the pellets were re-suspended in 0.15M NaCl and centrifuged again.
Central Composite Design Minitab
The supernatant was discarded and each tube containing the cell mass was dried at 60° C for 24 h and weighed to get the dry cell weight. Experimental Designs and Range of Treatment FactorsWe used a central composite design consisting of a factorial treatment structure, including a total number of treatment combinations N = 2 K + 2K + n 0.
K is the number of treatment factors, n0 is the number of replicates of treatment combinations at the center (n 0 1), and 2 is the number of axial points of the axis of each treatment factor, at a distance of α (α = 2 K/4) from the design center (, ). We used three treatment factors: temperature, initial pH of medium, and agitation (k = 3), six replicates of the center point combination (n 0 = 6), six star points, and α = 1.682.
This resulted in 20 test series, as shown in. The levels of the treatment factors are shown in. Plot of Actual and RSM-Predicted Values of Hib Biomass ProductionThe above polynomial model is expressed as 3-dimentional response surface graphs, indicating the maximum DCW values and the optimum values of the related explanatory variables. The maximum obtained DCW was about 5471 mg/L. The optimum values of the three treatment factors were agitation 250 rpm, temperature 35° C, and initial pH 8.5.
Shows the actual Hib DCW values measured based on the experiments and those values predicted by the RSM model. Effect of pH and TemperatureWith reference to ANOVA data , the pH of culture medium and temperature of incubation are very effective factors in the growth of Hib (p-value equal.
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Effect of Temperature and Initial pH Interactionand illustrate the 3-D response surfaces that show the effects of temperature and pH. Hib biomass production increased considerably when initial pH increased from 6 to 8.5 and temperature decreased to 35°C. When initial pH was less than the optimum point and tended towards 6, and agitation had fallen toward minimum values (about 100), Hib biomass production decreased parallel to decreasing temperature, from 39° to 35°C. At higher values of agitation (over 200 rpm), there was no significant difference between the amounts of Hib biomass produced at temperatures from 35°C to 39°C.
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However, when the initial pH was 8.5, decreasing incubation temperature from 39°C to 35°C led to substantially increased Hib biomass. Effect of temperature (°C) and pH on Hib Biomass (mg/l) Production Under Agitation at 250 rpmDespite the extensive studies that have been done on Hib, published studies on Hib cultivation are rare (, ), especially on the statistical optimization of physical and chemical factors affecting growth and bulk production of Hib biomass. Over the past years there has been only one published article using a reliable statistical method (Plackett-Burman Design) for optimization of Hib culture medium components. Nevertheless, Takagi and her colleagues published several very valuable articles on improvement and characterization of Hib PRP production (, ). Also we found that by using statistical methods like RSM and CCD to sketch an optimization plan, there will be a huge savings in the number and type of essential experiments, materials, time, depreciation of equipment and devices, human resources and specialists, and consumed energy, that will finally result in a lower overall price of the vaccine.