Continuous production of large amounts of monoclonal immunoglobulins in hollow fibers using protein-free medium

The performance of a protein-free medium was compared in culture flasks with a serum-supplemented medium and with a serum free medium in terms of cell growth and monoclonal antibody production by a murine hybridoma. We present results of continuous production in hollow fiber culture systems using serum-free medium and protein-free medium. In protein-free medium, it has been possible to produce large quantities of monoclonal antibody with a productivity similar to that obtained in serum-free medium. After a two steps purification process, monoclonal antibodies were characterized by SDS-PAGE, High Performance Size Exclusion Chromatography and Free Solution Capillary Electrophoresis. SDS-PAGE and high performance chromatography analysis have showed that purified monoclonal antibodies produced in serum-free medium or protein-free medium were similar. Furthermore, Capillary Electrophoresis characterization revealed that both MAbs were constituted by three isoforms with equivalent electrophoretic mobilities.Abbreviations CHES 2-(N-Cyclohexylamino)ethane-sulfonic acid - ECS Extracapillary Space - FSCE Free Solution Capillary Electrophoresis - HPSEC High Performance Size Exclusion Chromatography - ICS Intracapillary Space - MAb Monoclonal Antibody - PFM Protein-Free Medium - SFM Serum-Free Medium - SSM Serum-Supplemented Medium     

Strategies for enhancing monoclonal antibody accumulation in plant cell and organ cultures.

Various strategies aimed at improving IgG(1) antibody accumulation in transgenic tobacco cell and organ cultures were tested. The form of tissue had a significant effect on antibody levels; shooty teratomas were less productive than hairy roots or suspended cells. Although there were several disadvantages associated with hairy roots compared with suspensions, such as slower growth, slower antibody production, and formation of a greater number of antibody fragments, the roots exhibited superior long-term culture stability. Antibody accumulation in hairy root cultures was improved by increasing the dissolved oxygen tension to 150% air saturation, indicating the need for effective oxygen transfer in root reactors used for antibody production. Preventing N-linked glycosylation using tunicamycin or inhibition of subsequent glycan processing by castanospermine reduced antibody accumulation in the biomass and/or medium in cell suspensions. Loss of antibody from the cultures after its secretion and release into the medium was identified as a major problem. This effect was minimized by inhibiting protein transport in the secretory pathway using Brefeldin A, resulting in antibody accumulation levels up to 2.7 times those in untreated cells. Strategies for protecting secreted antibody, such as addition of poly(vinylpyrrolidone) and periodic harvesting from the medium using hydroxyapatite resin, also increased antibody titers. The mechanisms responsible for the disappearance of antibody from plant culture media were not clearly identified; degradation by proteases and conformational modification of the antibody, such as formation of aggregates, provided an explanation for some but not all the phenomena observed. This work demonstrates that the manipulation and control of culture conditions and metabolic processes in plant tissue cultures can be used to improve the production of foreign proteins. However, loss of secreted antibody from plant culture medium is a significant problem that may limit the feasibility of using product recovery from the medium to reduce downstream processing costs relative to agricultural systems.     

Evaluation of a simple protein free medium that supports high levels of monoclonal antibody production

A simple protein free medium was formulated and tested in suspension culture using three hybridoma cell lines. The medium, referred to as CDSS (Chemically Defined Serum Substitutes), consisted of the basal medium DMEM:Ham F12, 1:1, with HEPES (D12H), plus pluronic F68, trace elements, ferric citrate, ascorbic acid, and ethanolamine. No protein or lipid components were added. All three cell lines were weaned off serum using CDSS and a commercially available protein free medium PFHM-II. Data shown here indicated that normally cells took 1–7 weeks to wean off serum and an additional 2–7 weeks to adapt to suspension culture. After adaptation the cells were able to grow well in suspension culture using both protein free media and in the main performed better than serum containing controls. The stability of the three hybridoma cells for antibody production following freeze/thaw procedures and long term subculturing was also tested. All three lines were frozen using our protein free CDSS medium (containing 0.75% bovine serum albumin and 10% dimethyl sulfoxide) in liquid nitrogen for up to one year. Cells thawed from these stocks recovered well and were able to maintain good growth and antibody production characteristics. One line was shown to grow using our protein free CDSS medium in suspension culture for 12 weeks without loss of antibody productivity.     

Use of hollow fiber systems for rapid and direct scale up of antibody production from hybridoma cell lines cultured in CL-1000 flasks using BD Cell MAb medium

The combination of BD Cell MAb medium with the CL-1000 flask is increasingly being used to generate a few hundred milligram of antibody for early stage research projects. Cells are inoculated at 2 million per ml, and the antibody is harvested after 15 days or when the antibody concentration reaches above 10 mg ml⁻¹, whichever comes first. Currently, there is no means to scale up beyond this production level using this technology. In this study, we evaluated hollow fiber technology as the scale up alternative. The hollow fiber system was run in batch mode to mimic the method used for the CL-1000 with BD MAb medium. The FL-NS murine hybridoma cell line was simultaneously inoculated at 2 million cells per ml in a CL-1000 and the Maximizer hollow fiber bioreactor system, a 21-fold theoretical scale up over the CL-1000. The Maximizer produced 23-fold more antibody, very close to the expected theoretical amount. However, production was complete after 9 days in the Maximizer, while the CL-1000 required the full 15 days for production. In summary, these results demonstrate successful scale up of antibody production from the CL-1000 to a hollow fiber system. This revised version was published online in July 2006 with corrections to the Cover Date.     

Rapid monitoring of recombinant antibody production by mammalian cell cultures using fourier transform infrared spectroscopy and chemometrics

Fourier transform infrared (FT‐IR) spectroscopy combined with multivariate statistical analyses was investigated as a physicochemical tool for monitoring secreted recombinant antibody production in cultures of Chinese hamster ovary (CHO) and murine myeloma non‐secreting 0 (NS0) cell lines. Medium samples were taken during culture of CHO and NS0 cells lines, which included both antibody‐producing and non‐producing cell lines, and analyzed by FT‐IR spectroscopy. Principal components analysis (PCA) alone, and combined with discriminant function analysis (PC‐DFA), were applied to normalized FT‐IR spectroscopy datasets and showed a linear trend with respect to recombinant protein production. Loadings plots of the most significant spectral components showed a decrease in the C–O stretch from polysaccharides and an increase in the amide I band during culture, respectively, indicating a decrease in sugar concentration and an increase in protein concentration in the medium. Partial least squares regression (PLSR) analysis was used to predict antibody titers, and these regression models were able to predict antibody titers accurately with low error when compared to ELISA data. PLSR was also able to predict glucose and lactate amounts in the medium samples accurately. This work demonstrates that FT‐IR spectroscopy has great potential as a tool for monitoring cell cultures for recombinant protein production and offers a starting point for the application of spectroscopic techniques for the on‐line measurement of antibody production in industrial scale bioreactors. Biotechnol. Bioeng. 2010; 106: 432–442. © 2010 Wiley Periodicals, Inc.     

Biphasic culture strategy based on hyperosmotic pressure for improved humanized antibody production in Chinese hamster ovary cell culture

Hyperosmotic pressure increased specific antibody productivity (q(Ab)) of recombinant Chinese hamster ovary (rCHO) cells (SH2-0.32) and it depressed cell growth. Thus, the use of hyperosmolar medium did not increase the maximum antibody concentration substantially. To overcome this drawback, the feasibility of biphasic culture strategy was investigated. In the biphasic culture, cells were first cultivated in the standard medium with physiological osmolality (294 mOsm/kg) for cell growth. When cells reached the late exponential growth phase, the spent standard medium was replaced with the fresh hyperosmolar medium (522 mOsm/kg) for antibody production. The q(Ab) in growth phase with the standard medium was 2.1 microg per 10(6) cells/d, whereas the q(Ab) in antibody production phase with the hyperosmolar medium was 11.1 microg per 10(6) cells/d. Northern blot analysis showed a positive relationship between the relative contents of intracellular immunoglobulin messenger ribonucleic acid and q(Ab). Because of the enhanced q(Ab) and the increased cell concentration in biphasic culture, the maximum antibody concentration obtained in biphasic culture with 522 mOsm/kg medium exchange was 161% higher than that obtained in batch culture with the standard medium. Taken together, the simple biphasic culture strategy based on hyperosmotic culture is effective in improving antibody production of rCHO cells.     

Enhancement of antibody production by growth factor addition in perfusion and hollow-fiber culture systems

The effects of the high-molecular-weight growth factors, transferrin and bovine serum albumin (BSA), on antibody production were analyzed quantitatively in continuous hollow-fiber cultivation over a period of 60 days. Transferrin enhanced cell growth but had no significant effect on the specific antibody production rate, whereas BSA significantly enhanced antibody production. The antibody production rate was increased 4- and 14-fold respectively by feeding BSA at 2 and 5 g L(-1) into the EC side of the system (the side connected to the cell-containing outer part of the hollow-fiber unit) compared with the production achieved without BSA. Addition of 5 g L(1) BSA into the IC side of the system (the side connected to the inner part of the hollow-fiber unit) resulted in a 2.5-fold increase in the antibody production rate. The effect of BSA was also analyzed using the perfusion culture system with a separation unit. When fresh medium containing either 2 or 5 g L(-1) BSA was fed into the reactor, both the specific growth rate and specific death rate increased, while the specific antibody production rate was increased 2- and 25-fold, respectively, by feeding BSA at these two concentrations compared with no addition. Comparing the two systems, the increase in the antibody production rate achieved with the hollow-fiber system was threefold greater than that in the perfusion culture system with the same concentration of BSA feeding. (c) 1995 John Wiley & Sons, Inc.     

Peptone,a low-cost growth-promoting nutrient for intensive animal cell culture

The effect of addition of peptone to serum-free and serum supplemented media for the growth of hybridoma cells in various systems was studied. Supplementation of defined medium with either proteose peptone or meat peptone resulted in significant increases in cell number and specific monoclonal antibody production in batch culture system. Other peptones were either inactive or less effective. In continuous culture, using medium supplemented with new born calf serum, the addition of peptone resulted in 125% and 150% increases in cell and antibody concentrations respectively. Similar increase in cell number (128%) was also obtained in spin-filter perfusion culture when medium was supplemented with peptone. By comparison, the substitution of a defined 1xMEM amino acids mixture resulted in only a 50% increase. At higher perfusion rates the cell number maintained in steady state using peptone supplement could be increased to 1.3×10⁷ cells ml^–1 while the serum concentration was reduced from 5% to 1% at a perfusion rate of 2.5 volumes per day.     

Changes in monoclonal antibody productivity of recombinant BHK cells immobilized in collagen gel particles

Animal cell perfusion high density culture is often adopted for the production of biologicals in industry. In high density culture sometimes the productivity of biologicals has been found to be enhanced. Especially in immobilized animal cell culture, significant increase in the productivity has been reported. We have found that the specific monoclonal antibody (MAb) productivity of an immobilized hybridoma cell is enhanced more than double. Several examples of enhancing productivities have been also shown by collagen immobilized cells. Immobilized cells involve some different points from non-immobilized cells in high density culture: In immobilized culture, some cells are contacted together, resulting in locally much higher cell concentration more than 10⁸ cells/ml. Information originating from a cell can be easily transduced to the others in immobilized culture because the distance between cells is much nearer. Here we have performed collagen gel immobilized culture of recombinant BHK cells which produce a human IgG monoclonal antibody in a protein-free medium for more than three months. In this high density culture a stabilized monoclonal antibody production was found with around 8 times higher specific monoclonal antibody productivity compared with that in a batch serum containing culture. No higher MAb productivity was observed using a conditioned medium which was obtained from the high density culture, indicating that no components secreted from the immobilized cells work for enhancing monoclonal antibody production. The MAb productivity by the non-immobilized cells obtained by dissolving collagen using a collagenase gradually decreased and returned to the original level in the batch culture using a fresh medium. This suggests that the direct contact of the cells or a very close distance between the cells has something to do with the enhancement of the MAb productivity, and the higher productivity is kept for a while in each cell after they are drawn apart.     

Enhanced production of human monoclonal antibodies by the use of fructose in serum-free hybridoma culture media

It was found that the production of human monoclonal antibodies (MoAbs) by human-human hybridomas can be significantly enhanced by replacing glucose with fructose in the dish culture medium. Optimization of initial concentrations of fructose and glutamine, another influencing factor for MoAb production, enabled an enhanced production of human MoAb 2.1 times higher than that obtained using the conventional culture media employing glucose. It was shown by kinetic analysis that enhanced MoAb production at the optimum fructose concentration can be attributed to the retention of high specific antibody production rates and diminished time lag during the course of culture.These dish culture results with fructose-containing medium were successfully applied to the continuous perfusion culture with a slight modification, where 2.9- and 1.9-fold enhancements in specific antibody production rate and MoAb concentration, respectively, were attained as compared with the conventional glucose-containing medium.An inverse relationship was observed between the secreted concentrations of lactic acid and MoAb when the hybridoma was cultured in the media containing varying concentrations of fructose, i.e., the lower the lactic acid concentration, the higher the MoAb production andvice versa, suggesting that fructose at appropriate concentrations in the medium can serve as an alternative sugar for the efficient production of human MoAbs, with reduced pH shifts, for the serum-free culture of human-human hybridomas.     

Design of serum-free medium for suspension culture of CHO cells on the basis of general commercial media

The design of serum-free media for suspension culture of genetically engineered Chinese hamster ovary (CHO) cells using general commercial media as a basis was investigated. Subcultivation using a commercial serum-free medium containing insulin-like growth factor (IGF)-1 with or without FCS necessitated additives other than IGF-1 to compensate for the lack of FCS and improve cell growth. Suspension culture with media containing several combinations of growth factors suggested the effectiveness of addition of both IGF-1 and the lipid signaling molecule lysophosphatidic acid (LPA) for promoting cell growth. Subcultivation of CHO cells in suspension culture using the commercial serum-free medium EX-CELL™302, which contained an IGF-1 analog, supplemented with LPA resulted in gradually increasing specific growth rate comparable to the serum-containing medium and in almost the same high antibody production regardless of the number of generations. The culture with EX-CELL™302 supplemented with LPA in a jar fermentor with pH control at 6.9 showed an apparently higher cell growth rate than the cultures without pH control and with pH control at 6.8. The cell growth in the medium supplemented with aurintricarboxylic acid (ATA), which was much cheaper than IGF-1, in combination with LPA was synergistically promoted similarly to that in the medium supplemented with IGF-1 and LPA. In conclusion, the serum-free medium designed on the basis of general commercial media could support the growth of CHO cells and antibody production comparable to serum-containing medium in suspension culture. Moreover, the possibility of cost reduction by the substitution of IGF-1 with ATA was also shown.     

无牛血清IgG细胞培养基（—GFCS培养基）的制备及其在杂交瘤细胞体外培养中的应用

为了制备不含牛血清IgG的细胞培养基（－GFCS培养基）,并研究其在杂交瘤细胞体外培养中的应用,采用蛋白G亲和层析的方法,将含有血清的细胞培养基中的牛血清IgG去除,以制备无IgG的培养基。使用该培养基体外培养杂交瘤细胞后,监测细胞生长和上清抗体浓度。对培养上清中的IgG类单克隆抗体可以采用蛋白G亲和层析进行纯化。与示去除牛血清IgG的培养基相比,－GFCS培养基培养的杂交瘤细胞的生长状况及上清抗体浓度均无明显变化;从－GFCS培养上清中成功纯化出不被血清IgG污染的IgG类单克隆抗体,本文结果表明,采用－GFCS培养基体外培养分泌IgG类单抗的杂交瘤细胞,可以简化上清抗体的纯化工艺。     

Comparison of culture methods for human-human hybridomas secreting anti-HBsAg human monoclonal antibodies

Human-human hybridomas which secrete a human monoclonal antibody (h-MoAb) against hepatitis B virus surface antigen showed growth associated production kinetics. The rate of h-MoAb production rapidly decreased after cell growth was arrested in a perfusion culture, even if the perfusion rate was increased. A continuous suspended-perfusion culture, in which both culture broth and culture supernatant are continuously harvested and the same volume of fresh medium is continuously fed into the reactor, was developed to maintain continuous growing conditions during cultivation. In this culture system, the production of h-MoAb continued for more than 50 days with an average productivity of 5.0 mg/l of working volume/day. A semicontinuous immobilized-perfusion culture in which parts of the cells are repeatedly removed from the immobilized reactor was another useful technique for the long term cultivation of these h-h hybridomas. As an average h-MoAb production rate, 62 mg/l of immobilized-bed volume/day was achieved for 65 days of cultivation using a ceramic matrix reactor, and 327 mg/l/day was achieved over 47 days of cultivation using a hollow fiber reactor equipped with Cultureflo M^TM Thus, the antibody productivity per reactor volume per day by the semicontinuous immobilized-perfusion culture was much higher than that of the continuous perfusion culture in an agitation reactor.     

Long-term perfusion culture of hybridoma: a "grow or die" cell cycle system

In order to elucidate the hybridoma life cycle and the limiting factors in perfusion systems, we performed cultures in a stirred tank bioreactor, coupled to an external tangential flow filtration unit. Cell density and antibody production in perfusion were consistent with previous studies. The average life span of the cells (2.1-2.2 days), antibody, productivity per cell produced (30-38 mg/10(9) cells) and cell size diameter evolution appeared similar to values observed in batch cultures. These observations highly suggest a similar "grow or die" life cycle. Cell and antibody production, strictly related to the medium perfusion rate, seem to be under the control of the nutrient availability. A hypothesis to explain such a life cycle of hybridoma cells in perfusion systems and a model for viable and dead cell density is proposed.     

Long-term culture of human aortas

Summary Segments of human thoracic aorta were maintained in long-term explant culture for 18 weeks in serum-supplemented medium. The aortas were grossly normal in appearance, and random samples fixed for light microscopy prior to culture revealed a normal morphology. The intima contained no more than five layers of smooth muscle cells. After 7 days in culture, the intima was noticeably thicker than the uncultured segments. The increased thickness was due to proliferating smooth muscle cells and production of extracellular material. After several months in culture, extracellular material consisting of collagen and flocculent material was present in areas resembling atherosclerotic fibrous plaques. A peripheral growth, which formed around the explant, was composed of fibroblastlike cells and added to the overall thickness of the intima. However, aortic segment maintained for up to 2 months in serum-free culture medium showed no cellular proliferation. This study demonstrates that changes resembling early stages of atherosclerosis occur in human aortas maintained in explant culture using routine culture procedures. Supported in part by the Pangborn Fund and the Graduate School of the University of Maryland. This is publication 443 from the Cellular Pathobiology Laboratory.     

Facile development of medium optimization for antibody production: implementation in spinner flask and hollow fiber reactor

Most bio-industrial mammalian cells are cultured in serum-free media to achieve advantages, such as batch consistency, suspended growth, and simplified purification. The successful development of a serum-free medium could contribute to a reduction in the experimental variation, enhance cell productivity, and facilitate biopharmaceuticals production using the cell culture process. Commercial serum-free media are also becoming more and more popular. However, the cell line secrets its own recombinant product and has special nutritional requirements. How can the composition of the proprietary medium be adjusted to support the specific cell’s metabolism and recombinant protein? This article uses statistical strategies to modify the commercial medium. A design of experiments is adopted to optimize the medium composition for the hybridoma cell in a serum-free condition. The supplements of peptone, ferric citrate, and trace elements were chosen to study their impact on hybridoma growth and antibody production using the response surface methodology. The stimulatory effect of the developed formulation on hybridoma growth was confirmed by the steepest ascent path. The optimal medium stimulated the hybridoma growth and antibody production in three diverse systems: a static plate, an agitated spinner flask, and a hollow fiber reactor. The cells in the developed serum-free medium had a better antibody production as compared to that in the commercial medium in the hollow fiber reactor. Our results demonstrated that the facile optimization for medium and antibody production was successfully accomplished in the hybridoma cells.     

Raman-based dynamic feeding strategies using real-time glucose concentration monitoring system during adalimumab producing CHO cell cultivation

The use of Process Analytical Technology tools coupled with chemometrics has been shown great potential for better understanding and control of mammalian cell cultivations through real-time process monitoring. In-line Raman spectroscopy was utilized to determine the glucose concentration of the complex bioreactor culture medium ensuring real-time information for our process control system. This work demonstrates a simple and fast method to achieve a robust partial least squares calibration model under laboratory conditions in an early phase of the development utilizing shake flask and bioreactor cultures. Two types of dynamic feeding strategies were accomplished where the multi-component feed medium additions were controlled manually and automatically based on the Raman monitored glucose concentration. The impact of these dynamic feedings was also investigated and compared to the traditional bolus feeding strategy on cellular metabolism, cell growth, productivity, and binding activity of the antibody product. Both manual and automated dynamic feeding strategies were successfully applied to maintain the glucose concentration within a narrower and lower concentration range. Thus, besides glucose, the glutamate was also limited at low level leading to reduced production of inhibitory metabolites, such as lactate and ammonia. Consequently, these feeding control strategies enabled to provide beneficial cultivation environment for the cells. In both experiments, higher cell growth and prolonged viable cell cultivation were achieved which in turn led to increased antibody product concentration compared to the reference bolus feeding cultivation.     

甲醇-山梨醇混合碳源诱导提高抗HER2抗体在糖基工程毕赤酵母中的表达

目的：以抗HER2抗体为模型,研究抗体在糖基工程酵母菌中的表达及工程菌发酵技术。方法：首先通过摇瓶试验分析诱导用甲醇浓度对抗体表达的影响,并用高表达HER2的SK-BR-3细胞分析抗HER2抗体的抗原结合活性。以此为基础,在5 L发酵罐中研究甲醇-山梨醇混合碳源流加诱导对抗HER2抗体表达水平的影响;收集发酵培养液,采用阳离子交换层析对目标产物进行纯化;利用SDS-PAGE、Western印迹、Lowry法对抗体的相对分子质量、浓度等进行分析。结果：摇瓶试验结果表明,甲醇浓度为0.5%时抗体表达量最高,且糖基工程毕赤酵母菌表达的抗HER2抗体具有与SK-BR-3细胞抗原结合的活性;在5 L发酵罐中,利用甲醇和山梨醇混合诱导方式发酵表达抗体,其表达量可提高至0.6 g/L,比摇瓶诱导表达的抗体产量提高了近10倍;非还原SDS-PAGE及Western印迹表明抗体相对分子质量为1.5×105,与商业化抗体Herceptin的大小一致;经过一步阳离子交换层析纯化,纯化后抗体浓度为0.365 g/L。结论：采用甲醇-山梨醇混合碳源诱导方式在5 L发酵罐中进行发酵表达,能够提高抗HER2抗体在糖基工程酵母菌中的表达量,本研究可为抗体在酵母中的规模发酵技术提供重要参考。     

A new serum-free medium for monoclonal antibody production

A new serum-free, defined-protein, medium for the growth of murine hybridoma cells and the production of monoclonal antibodies has been developed. Designated WRC 935 medium, this formulation supports the growth of hybridoma cells in higher numbers, and promotes better cell viabilities and increased monoclonal antibody levels compared to growth in DMEM supplemented with 10% fetal bovine serum or in a DMEM/F-12 serum-free mixture. In suspension cultures, WRC 935 medium typically promoted cell growth to densities over two million cells per milliliter. This medium also promoted the rapid growth of cells following their transfer from liquid nitrogen storage. WRC 935 medium is especially useful for high density cell culture production methods using hollow-fiber bioreactors. Hollow-fiber bioreactors using this medium produced antibody at an average rate of 11 mg/day, and the antibody concentration ranged from 10 to 40 mg/ml.     

Effects of cell culture conditions on antibody N‐linked glycosylation—what affects high mannose 5 glycoform

The glycosylation profile of therapeutic antibodies is routinely analyzed throughout development to monitor the impact of process parameters and to ensure consistency, efficacy, and safety for clinical and commercial batches of therapeutic products. In this study, unusually high levels of the mannose‐5 (Man5) glycoform were observed during the early development of a therapeutic antibody produced from a Chinese hamster ovary (CHO) cell line, model cell line A. Follow up studies indicated that the antibody Man5 level was increased throughout the course of cell culture production as a result of increasing cell culture medium osmolality levels and extending culture duration. With model cell line A, Man5 glycosylation increased more than twofold from 12% to 28% in the fed‐batch process through a combination of high basal and feed media osmolality and increased run duration. The osmolality and culture duration effects were also observed for four other CHO antibody producing cell lines by adding NaCl in both basal and feed media and extending the culture duration of the cell culture process. Moreover, reduction of Man5 level from model cell line A was achieved by supplementing MnCl₂ at appropriate concentrations. To further understand the role of glycosyltransferases in Man5 level, N‐acetylglucosaminyltransferase I GnT‐I mRNA levels at different osmolality conditions were measured. It has been hypothesized that specific enzyme activity in the glycosylation pathway could have been altered in this fed‐batch process. Biotechnol. Bioeng. 2011;108: 2348–2358. © 2011 Wiley Periodicals, Inc.