Impact of NH4+ nitrogen source on the production of Rhizopus oryzae lipase in Pichia pastoris

BackgroundPichia pastoris is a highly successful system for heterologous expression. During the induction stage, the ammonium ion released into the fermentation broth has a deep impact on cell growth and protein expression. The impact of NH₄⁺ concentration on the expression of the Rhizopus oryzae lipase proAROL in P. pastoris was investigated.ResultsThe lipase activity under the optimum NH₄⁺ concentration of 440 mmol/L reached 12,019 U/mL. Increased concentrations of NH₄⁺ in the broth prevented the protease production, resulting in higher specific lipase activity in the supernatant. Furthermore, analysis of carbon metabolism and energy regeneration pattern revealed that under the definite NH₄⁺ concentrations more carbon source (methanol) was consumed with surged AOX activity and then the higher energy and amino acid precursors demand for recombinant protein synthesis is compensated for by the TCA cycle.ConclusionsIn this study, the R. oryzae lipase activity reaches the highest level ever reported under optimized NH₄⁺ concentration and the analysis of the carbon metabolism provides useful information for future optimization of protein production by P. pastoris in a molecular level.     

Overexpression of Candida rugosa lipase Lip1 via combined strategies in Pichia pastoris

In this study, combined strategies were employed to heterologously overexpress Candida rugosa lipase Lip1 (CRL1) in a Pichia pastoris system. The LIP1 gene was systematically codon-optimized and synthesized in vitro. The Lip1 activity of a recombinant strain harboring three copies of the codon-optimized LIP1 gene reached 1200 U/mL in a shake flask culture. Higher lipase activity, 1450 U/mL, was obtained using a five copy number construct. Co-expressing one copy of the ERO1p and BiP chaperones with Lip1p, the CRL1 lipase yield further reached 1758 U/mL, which was significantly higher than that achieved by expressing Lip1p alone or only co-expressing one molecular chaperone. When cultivated in a 3 L fermenter under optimal conditions, the recombinant strain GS115/87-ZA-ERO1p-BiP #7, expressing the molecular chaperones Ero1p and BiP, produced 13,490 U/mL of lipase activity at 130 h, which was greater than the 11,400 U/mL of activity for the recombinant strain GS115/pAO815-α-mCRL1 #87, which did not express a molecular chaperone. This study indicates that a strategy of combining codon optimization with co-expression of molecular chaperones has great potential for the industrial-scale production of pure CRL1.     

基因拷贝数和甲醇浓度对重组毕赤酵母产华根霉脂肪酶的影响

将华根霉脂肪酶基因克隆到甲基营养型毕赤酵母中表达,以甲醇利用快型菌株为宿主,在7 L发酵罐水平对脂肪酶基因拷贝数分别为3、5、6的3株基因重组菌——XY RCL-3、XY RCL-5、XY RCL-6进行高密度发酵调控,同时研究了甲醇浓度对表达华根霉脂肪酶的影响。结果表明,XY RCL-5在相同条件下发酵产酶能力高于XY RCL-6和XY RCL-3,最适甲醇诱导浓度控制在0.1%±0.02%时,酶活可达到12 500 U/mL,菌体干重达到204 g/L,蛋白浓度也能达到8.02 g/L。     

Biocatalytic potential of lipase from Staphylococcus sp. MS1 for transesterification of jatropha oil into fatty acid methyl esters

An extracellular lipase producing isolate Staphylococcus sp. MS1 was optimized for lipase production and its biocatalytic potential was assessed. Medium with tributyrin (0.25 %) and without any exogenous inorganic nitrogen source was found to be optimum for lipase production from Staphylococcus sp. MS1. The optimum pH and temperature for lipase production were found to be pH 7 and 37 °C respectively, showing lipase activity of 37.91 U. It showed good lipase production at pH 6–8. The lipase was found to be stable in organic solvents like hexane and petroleum ether, showing 98 and 88 % residual activity respectively. The biotransformation using the concentrated enzyme in petroleum ether resulted in the synthesis of fatty acid methyl esters like methyl oleate, methyl palmitate and methyl stearate. Thus, the lipase under study has got the potential to bring about transesterification of oils into methyl esters which can be exploited for various biotechnological applications.     

Metabolic engineering of Pichia pastoris for malic acid production from methanol

The application of rational design in reallocating metabolic flux to accumulate desired chemicals is always restricted by the native regulatory network. In this study, recombinant Pichia pastoris was constructed for malic acid production from sole methanol through rational redistribution of metabolic flux. Different malic acid accumulation modules were systematically evaluated and optimized in P. pastoris. The recombinant PP‐CM301 could produce 8.55 g/L malic acid from glucose, which showed a 3.45‐fold increase compared to the parent strain. To improve the efficiency of site‐directed gene knockout, NHEJ‐related protein Ku70 was destroyed, whereas leading to the silencing of heterogenous genes. Hence, genes related to by‐product generation were deleted via a specially designed FRT/FLP system, which successfully reduced succinic acid and ethanol production. Furthermore, a key node in the methanol assimilation pathway, glucose‐6‐phosphate isomerase was knocked out to liberate metabolic fluxes trapped in the XuMP cycle, which finally enabled 2.79 g/L malic acid accumulation from sole methanol feeding with nitrogen source optimization. These results will provide guidance and reference for the metabolic engineering of P. pastoris to produce value‐added chemicals from methanol.     

Optimization of norovirus virus‐like particle production in Pichia pastoris using a real‐time near‐infrared bioprocess monitor

The production of norovirus virus‐like particles (NoV VLPs) displaying NY‐ESO‐1 cancer testis antigen in Pichia pastoris BG11 Mut⁺ has been enhanced through feed‐strategy optimization using a near‐infrared bioprocess monitor (RTBio^® Bioprocess Monitor, ASL Analytical, Inc.), capable of monitoring and controlling the concentrations of glycerol and methanol in real‐time. The production of NoV VLPs displaying NY‐ESO‐1 in P. pastoris has potential as a novel cancer vaccine platform. Optimization of the growth conditions resulted in an almost two‐fold increase in the expression levels in the fermentation supernatant of P. pastoris as compared to the starting conditions. We investigated the effect of methanol concentration, batch phase time, and batch to induction transition on NoV VLP‐NY‐ESO‐1 production. The optimized process included a glycerol transition phase during the first 2 h of induction and a methanol concentration set point of 4 g L^?1 during induction. Utilizing the bioprocess monitor to control the glycerol and methanol concentrations during induction resulted in a maximum NoV VP1‐NY‐ESO‐1 yield of 0.85 g L^?1. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:518–526, 2016     

Increasing Secretion of a Bivalent Anti-T-Cell Immunotoxin by Pichia pastoris

The bivalent anti-T-cell immunotoxin A-dmDT390-bisFv(G₄S) was developed for treatment of T-cell leukemia and autoimmune diseases and for tolerance induction for transplantation. This immunotoxin was produced extracellularly in toxin-sensitive Pichia pastoris JW102 (Mut⁺) under control of the AOX1 promoter. There were two major barriers to efficient immunotoxin production, the toxicity of the immunotoxin for P. pastoris and the limited capacity of P. pastoris to secrete the immunotoxin. The immunotoxin toxicity resulted in a decrease in the methanol consumption rate, cessation of cell growth, and low immunotoxin productivity after the first 22 h of methanol induction. Continuous cell growth and continuous immunotoxin secretion after the first 22 h of methanol induction were obtained by adding glycerol to the methanol feed by using a 4:1 methanol-glycerol mixed feed as an energy source and by continuously adding a yeast extract solution during methanol induction. The secretory capacity was increased from 22.5 to 37 mg/liter by lowering the induction temperature. A low temperature reduced the methanol consumption rate and protease activity in the supernatant but not cell growth. The effects of adding glycerol and yeast extract to the methanol feed were synergistic. Adding yeast extract primarily enhanced methanol utilization and cell growth, while adding glycerol primarily enhanced immunotoxin production. The synergy was further enhanced by decreasing the induction temperature from 23 to 15°C, which resulted in a robust process with a yield of 37 mg/liter, which was sevenfold greater than the yield previously reported for a toxin-resistant CHO cell expression system. This methodology should be applicable to other toxin-related recombinant proteins in toxin-sensitive P. pastoris.     

Enhanced production of Thermomyces lanuginosus lipase in Pichia pastoris via genetic and fermentation strategies

This study attempted to enhance the expression level of Thermomyces lanuginosus lipase (TLL) in Pichia pastoris using a series of strategies. The tll gene was first inserted into the expression vector pPIC9 K and transformed into P. pastoris strain GS115. The maximum hydrolytic activity of TLL reached 4,350 U/mL under the optimal culture conditions of a 500 mL shaking flask containing 20 mL culture medium with the addition of 1.2 % (w/v) methanol, cultivation for 144 h at pH 7.0 and 27 °C. To further increase the TLL expression and copy number, strains containing two plasmids were obtained by sequential electroporation into GS115/9k-TLL #3 with a second vector, either pGAPZαA-TLL, pFZα-TLL, or pPICZαA-TLL. The maximum activity of the resultant strains GS115/9KTLL-ZαATLL #40, GS115/9KTLL-FZαATLL #46 and GS115/9KTLL-GAPTLL #45 was 6,600 U/mL, 6,000 U/mL and 4,800 U/mL, respectively. The tll copy number in these strains, as assessed by real-time quantitative PCR, was demonstrated to be seven, five, and three, respectively, versus two copies in GS115/9k-TLL #3. When a co-feeding strategy of sorbitol/methanol was adopted in a 3-L fermenter, the maximum TLL activity of GS115/9k-TLL #3 increased to 27,000 U/mL after 130 h of fed-batch fermentation, whereas, the maximum TLL activity was 19,500 U/mL after 145 h incubation when methanol was used as the sole carbon source.     

Secretion of pro- and mature Rhizopus arrhizus lipases by Pichia pastoris and properties of the proteins

The lipases of Rhizopus spp. share a high 1,3-regiospecificity toward triacylglycerols, which makes them important enzymes in lipid modification. In the present study, the extracellularly active production of recombinant Rhizopus arrhizus lipase was carried out with genes encoding the mature region (mRAL) and the mRAL having the prosequence (ProRAL) in Pichia pastoris. Two transformed P. pastoris clones containing the multicopy of mRAL and ProRAL genes were separately selected for the production of recombinant enzymes. In a fed-batch cultivation, where methanol feeding was controlled by an on-line methanol analyzer, the supernatant contained 91 mg/L recombinant pro-form lipase (rProRAL) and 80 mg/L recombinant mature lipase (rRAL) after 92 h of cultivation. rProRAL and rRAL were purified by ultrafiltration, SP-Sepharose Rast Flow chromatography, and Butyl-Sepharose Fast Flow chromatography. Molecular weights of rProRAL and rRAL are 32 kDa and 29 kDa, respectively. The amino-terminal analysis showed that the 32-kDa protein was mRAL attached with 28 amino acids of the carboxy-terminal part of the prosequence (rPro28RAL). The specific lipase activities of mRAL attached with 28 amino acids of the carboxy-terminal part of the prosequence (rPro28RAL) and rRAL were 1543 U/mg and 2437 U/mg. The rPro28RAL was more stable than rRAL at pH 4.0–7.0, whereas rRAL was more stable at pH 7.0–10.0. The rPro28RAL had the highest lipase activity toward tributyrin (C₄), whereas rRAL had the highest lipase activity toward tricaprylin (C₈).     

带His-tag的解脂耶氏酵母脂肪酶Lip2在毕赤酵母中的表达及纯化

将去自身信号肽并且N-端带6×His标签的YlLip2基因克隆至表达载体pPIC9K中,电转化GS115获得高效表达脂肪酶His₆-YlLip2的基因工程菌。筛选到的阳性克隆子摇瓶发酵脂肪酶活力最高为400U/ml。对重组毕赤酵母在10 L发酵罐中表达His₆-YlLip2的分批补料发酵工艺进行了初步优化,探讨了培养基、pH、温度对生物量和重组蛋白表达量的影响。结果表明:采用FM22培养基,诱导温度为25℃,pH 5.0,甲醇诱导114 h后His₆-YlLip2的最高酶活力达到3160U/ml。SDS-PAGE分析表明,蛋白的分子量大约为38kDa。重组的His₆-YlLip2经镍柱一步纯化后的纯度达到95.43%,比酶活达到4250U/mg。     

Improvement of cell-bound lipase from Rhodotorula mucilaginosa P11I89 for use as a methanol-tolerant, whole-cell biocatalyst for production of palm-oil biodiesel

Rhodotorula mucilaginosa P11I89, isolated from oil-contaminated soil, was effectively used as the methanol-tolerant, whole-cell lipase for the synthesis of fatty acid methyl ester (FAME) via transesterification reaction in the presence of palm oil and methanol substrates at a 1:6 mole ratio. A combination of Taguchi experimental design and response surface methodology (RSM) were applied to systemically enhance transesterification activity of the whole-cell lipase or cell-bound lipase (CBL) from R. mucilaginosa P11I89 in a solvent-free system. The significant impacts of four factors including carbon sources, nitrogen sources, surfactants and pH on hydrolysis activity of extracellular and cell-bound lipases, and on the transesterification activity of CBL were evaluated using Taguchi design. Gum Arabic was the most significant component for high transesterification activity, whereas soybean oil was the most influential factor for the hydrolysis activity. Maximal CBL production of 272.72 U/L was obtained in the cultivation medium containing 2.1 % palm oil, 0.2 % NH₄NO₃ , and 0.45 % Gum Arabic, with initial pH 5.0 under shaking speed of 200 rpm at a temperature of 30?±?2 °C after 60 h incubation using Central Composite Design (CCD). Yeast cells grown under such conditions increased FAME yield from 84.0 to 92.98 % when the transesterification reaction was carried out, in comparison to those cultivated in the initial medium.     

Acidic lipase Lip I.3 from a Pseudomonas fluorescens‐like strain displays unusual properties and shows activity on secondary alcohols

Aims

Identification, cloning, expression and characterization of a novel lipase – Lip I.3 – from strain Pseudomonas CR‐611.

Methods and Results

The corresponding gene was identified and isolated by PCR‐amplification, cloned and expressed in Escherichia coli, and purified by refolding from inclusion bodies. Analysis of the deduced amino acid sequence revealed high homology with members of the bacterial lipase family I.3, showing 97% identity to a putative lipase from Pseudomonas fluorescens Pf0‐1, and 93% identity to a crystallized extracellular lipase from Pseudomonas sp. MIS38. A typical C‐terminal type I secretion signal and several putative Ca²⁺ binding sites were also identified. Experimental data confirmed that Lip I.3 requires Ca²⁺ ions for correct folding and activity. The enzyme differs from the previously reported family I.3 lipases in optimal pH, being the first acidophilic lipase reported in this family. Furthermore, Lip I.3 shows a strong preference for medium chain fatty acid esters and does not display interfacial activation. When tested for activity on secondary alcohol hydrolysis, Lip I.3 displayed higher efficiency on aromatic alcohols rather than on alkyl alcohols.

Conclusions

A new family I.3 lipase with unusual properties has been isolated, cloned and described. This will contribute to a better knowledge of family I.3 lipases, a family that has been scarcely explored, and that might provide a novel source of biocatalysts.

Significance and Impact of the Study

The unusual properties shown by Lip I.3 and the finding of activity and enantioselectivity on secondary alcohol esters may contribute to the development of new enzymatic tools for applied biocatalysis.     

A new strategy for secretory expression and mixed fermentation of recombinant human collagen α1 (III) chain in Pichia pastoris

Recombinant human full-length mature collagen α1 (III) chain (rhCOL3A1) was secreted by Pichia pastoris GS115, using the Saccharmyces cerevisiae á-mating factor prepro signal, and the theoretical molecular weight of rhCOL3A1 was 95.344 kDa. The gene cloned from human placenta, was designed and cloned into expression vector pPIC9K under the control of a strong inducible promoter AOX1.The expression stage of rhCOL3A1 was sensitive to different carbon ratios through mixed fermentation. LCMS/ MS analysis and western blotting demonstrated that the recombinant human full-length mature collagen a1 (III) gene was successfully expressed in P. pastoris GS115 during the methanol induction stage. Furthermore, an effective strategy of mixed fermentation was established to express rhCOL3A1 in shake flash. Compared to single carbon induction, when induced with mixed carbon at the ration of 0.8 (glycerol/methanol), the time corresponding to the highest yield of rhCOL3A1 (1.27 g/L) was drastically reduced by 50%. The same conclusion was observed from RT-qPCR. Consequently, a new strategy which was more time-saving and effective was provided for the large-scale producing the full-length mature rhCOL3A1.     

Optimization of five environmental factors to increase beta‐propeller phytase production in Pichia pastoris and impact on the physiological response of the host

Recently, we engineered Pichia pastoris Mut^s strains to produce several beta‐propeller phytases, one from Bacillus subtilis and the others designed by a structure‐guided consensus approach. Furthermore, we demonstrated the ability of P. pastoris to produce and secrete these phytases in an active form in shake‐flask cultures. In the present work, we used a design of experiments strategy (Simplex optimization method) to optimize five environmental factors that define the culture conditions in the induction step to increase beta‐propeller phytase production in P. pastoris bioreactor cultures. With the optimization process, up to 347,682 U (82,814 U/L or 6.4 g/L culture medium) of phytase at 68 h of induction was achieved. In addition, the impact of the optimization process on the physiological response of the host was evaluated. The results indicate that the increase in extracellular phytase production through the optimization process was correlated with an increase in metabolic activity of P. pastoris, shown by an increase in oxygen demand and methanol consumption, that increase the specific growth rate. The increase in extracellular phytase production also occurred with a decrease in extracellular protease activity. Moreover, the optimized culture conditions increased the recombinant protein secretion by up to 88%, along with the extracellular phytase production efficiency per cell. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:1377–1385, 2013     

Improved production of polygalacturonate lyase by combining a pH and online methanol control strategy in a two-stage induction phase with a shift in the transition phase

Polygalacturonate lyase is a kind of enzyme that is abundantly used in the textile industry for cotton scouring. Previously, we reconstructed the polygalacturonate lyase gene in Pichia pastoris for the expression of this enzyme. To enhance the production of polygalacturonate lyase (PGL), a combined strategy was formulated by combining online methanol control and two-stage pH control strategies. For the two-stage pH control strategy during the growth phase, the pH was controlled at 5.5, and in the induction phase different pH levels were investigated for the optimum enzyme production. During the online methanol control strategy, the different levels of methanol (v/v) were investigated for the best enzyme production at pH 5.5. These two strategies were combined together for enhanced PGL productivity, and the induction phase was divided into two stages in which methanol concentrations were maintained at different levels online. The transition phase was introduced during the induction phase instead of introducing it after the growth phase. The two-stage combination strategy was formulated on the bases of methanol consumption of cells, optimal pH, cell viability and the production of polygalacturonate lyase by P. pastoris. By using this strategy, the production was doubled compared with common conditions, and the highest polygalacturonate lyase activity reached 1,631 U/ml. This strategy proved to be very useful for the enhancement of polygalacturonate lyase production by achieving higher cell viability, alcohol oxidase activity and phosphate-related compounds of the cells during the induction phase.     

Biochemical characterization and high-level production of oxidized polyvinyl alcohol hydrolase from Sphingopyxis sp. 113P3 expressed in methylotrophic Pichia pastoris

The Sphingopyxis sp. 113P3 gene oph, encoding oxidized polyvinyl alcohol hydrolase (OPH), was optimized with the preferred codons of Pichia pastoris and ligated into the pPIC9K vector behind the α-factor signal sequence. The vector was then transfected into P. pastoris GS115 and genomic integration was confirmed. Large-scale production of recombinant protein was performed by induction with 14.4 g/L methanol at 22 °C in a 3-L bioreactor. The maximal OPH activity obtained was 68.4 U/mL, which is the highest activity reported. The optimal pH and temperature of recombinant OPH were 8.0 and 45 °C, respectively. OPH activity was stable over a pH range of 5.0–8.5, and at a maximal temperature of 45 °C. The K _cat /K _m of recombinant OPH was 598 mM^?1 s^?1, which was 4.27-fold higher than that of recombinant OPH derived from Escherichia coli. The improved catalytic efficiency of OPH expressed in recombinant P. pastoris makes it favorable for industrial applications.     

Enhanced protein production by sorbitol co-feeding with methanol in recombinant <Emphasis Type="Italic">Pichia pastoris</Emphasis> strains

Pichia pastoris strains carrying 1, 6, 12, and 18 copies of the porcine insulin precursor (PIP) gene, were employed to investigate the effects of sorbitol co-feeding with methanol on the physiology of the strains. Multicopy clones of the methylotrophic yeast were generated to vary the PIP gene dosage and recombinant proteins. Elevated gene dosage increased levels of the recombinant PIP protein when methanol served as the sole carbon and energy source i.e., an increase of 1.9% for a strain carrying 1 copy, 42.6% for a strain carrying 6 copies, 34.7% for a strain carrying 12 copies and 80.9% for a strain carrying 18 copies, respectively (using sorbitol co-feeding with methanol during the induction phase). However, it had no significant influence on a lower gene dosage strain (1 copy), but this approach affirmed enhancement in cell growth and PIP production for higher gene dosage strain (6, 12, and 18 copies) via using sorbitol co-feeding with methanol. Additionally, the co-feeding strategy could hold vital importance for recombinant protein production by a multi-copy P. pastoris system.     

Fed-batch high-cell-density fermentation strategies for Pichia pastoris growth and production

Pichia pastoris is extensively used to produce various heterologous proteins. Amounts of biopharmaceutical drugs and industrial enzymes have been successfully produced by fed-batch high-cell-density fermentation (HCDF) of this cell factory. High levels of cell mass in defined media can be easily achieved and therefore large quantities of recombinant proteins with enhanced activities and lower costs can be obtained through HCDF technology. A robust HCDF process makes a successful transition to commercial production. Recently, efforts have been made to increase the heterologous protein production and activity by the HCDF of P. pastoris. However, challenges around selecting a suitable HCDF strategy exist. The high-level expression of a specific protein in P. pastoris is still, at least in part, limited by optimizing the methanol feeding strategy. Here, we review the progress in developments and applications of P. pastoris HCDF strategies for enhanced expression of recombinant proteins. We focus on the methanol induction strategies for efficient fed-batch HCDF in bioreactors, mainly focusing on various stat-induction strategies, co-feeding, and the limited induction strategy. These processes control strategies have opened the door for expressing foreign proteins in P. pastoris and are expected to enhance the production of recombinant proteins.     

Enhanced truncated-t-PA (CT-b) expression in high-cell-density fed-batch cultures of <Emphasis Type="Italic">Pichia pastoris</Emphasis> through optimization of a mixed feeding strategy by response surface methodology

Recently, Pichia pastoris has been the focal point of interest as an expression system for production of many recombinant proteins. The study and optimization of feeding strategy are of major importance to achieve maximum volumetric productivity in fed-batch cultivations. Among different feeding strategies used in P. pastoris fed-batch cultures, those trying to maintain a constant specific growth rate have usually resulted in superior productivities. The objective of the present study was to investigate and optimize the co-feeding of glycerol and methanol to attain maximum expression of t-PA in P. pastoris fed-batch cultures with constant specific growth rate. The experiments were designed by response surface methodology, considering the specific feeding rates of methanol and glycerol as independent variables. In each experiment, glycerol and methanol were fed according to a predetermined equation to maintain a constant specific growth rate. It was found that with glycerol feeding for higher specific growth rates, the inhibitory properties of glycerol are more pronounced, while the best expression level was achieved when the ratio of µ _set glycerol to that of methanol was around 1.67. In all specific growth rates tested, almost a similar ratio of the specific glycerol feeding rate to that of methanol led to the maximum protein production and activity. The statistical model predicted the optimal operating conditions for µ _set glycerol and that of methanol to be 0.05 and 0.03 h^?1, respectively. Applying the optimum strategy, maximum of 52 g/L biomass, 300 mg/L t-PA and 340,000 IU/mL enzyme activity were obtained.     

Candida rugosa lipase mediated multigram synthesis of acid part of S(+)-atliprofen,a new NSAID and molecular modeling studies aimed at predicting selectivity of the enzyme

An efficient procedure to prepare S-4-(3-thienyl)phenyl-α-methylacetic acid, an intermediate of a recently approved non-steroidal anti-inflammatory cyclooxygenase inhibitor atliprofen by enantioselective hydrolysis of the corresponding esters in presence of candida rugosa lipase is reported. The methyl and butyl esters of the racemic acid 2 were synthesized and subjected to enantioselective hydrolysis by the lipase to give S-4-(3-thienyl)phenyl-α-methylacetic acid upto 97.86% ee. The observed enantioselectivity during the hydrolysis of the substrate by the lipase was rationalized by molecular modeling studies. The methyl esters of both R and S-enantiomers of 4-(3-thienyl)phenyl-α-methylacetic acid, naproxen and ketoprofen were taken for the modeling studies. The results of the modeling studies are in conformity with the experimental observations.