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     

Techno‐economic analysis for incorporating a liquid–liquid extraction system to remove acetic acid into a proposed commercial scale biorefinery

Mitigating the effect of fermentation inhibitors in bioethanol plants can have a great positive impact on the economy of this industry. Liquid–liquid extraction (LLE) using ethyl acetate is able to remove fermentation inhibitors—chiefly, acetic acid—from an aqueous solution used to produce bioethanol. The fermentation broth resulting from LLE has higher performance for ethanol yield and its production rate. Previous techno‐economic analyses focused on second‐generation biofuel production did not address the impact of removing the fermentation inhibitors on the economic performance of the biorefinery. A comprehensive analysis of applying a separation system to mitigate the fermentation inhibition effect and to provide an analysis on the economic impact of removal of acetic acid from corn stover hydrolysate on the overall revenue of the biorefinery is necessary. This study examines the pros and cons associated with implementing LLE column along with the solvent recovery system into a commercial scale bioethanol plant. Using details from the NREL‐developed model of corn stover biorefinery, the capital costs associated with the equipment and the operating cost for the use of solvent were estimated and the results were compared with the profit gain due to higher ethanol production. Results indicate that the additional capital will add 1% to the total capital and manufacturing cost will increase by 5.9%. The benefit arises from the higher ethanol production rate and yield as a consequence of inhibitor extraction and results in a $0.35 per gallon reduction in the minimum ethanol selling price (MESP). © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:971–977, 2016     

Comparison of glucose/xylose cofermentation of poplar hydrolysates processed by different pretreatment technologies

The inhibitory effects of furfural and acetic acid on the fermentation of xylose and glucose to ethanol in YEPDX medium by a recombinant Saccharomyces cerevisiae strain (LNH‐ST 424A) were investigated. Initial furfural concentrations below 5 g/L caused negligible inhibition to glucose and xylose consumption rates in batch fermentations with high inoculum (4.5–6.0 g/L). At higher initial furfural concentrations (10–15 g/L) the inhibition became significant with xylose consumption rates especially affected. Interactive inhibition between acetic acid and pH were observed and quantified, and the results suggested the importance of conditioning the pH of hydrolysates for optimal fermentation performance. Poplar biomass pretreated by various CAFI processes (dilute acid, AFEX, ARP, SO₂‐catalyzed steam explosion, and controlled‐pH) under respective optimal conditions was enzymatically hydrolyzed, and the mixed sugar streams in the hydrolysates were fermented. The 5‐hydroxymethyl furfural (HMF) and furfural concentrations were low in all hydrolysates and did not pose negative effects on fermentation. Maximum ethanol productivity showed that 0–6.2 g/L initial acetic acid does not substantially affect the ethanol fermentation with proper pH adjustment, confirming the results from rich media fermentations with reagent grade sugars. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Production of conjugated linoleic acid by probiotic Lactobacillus acidophilus La-5

Aims:  To study the ability of the probiotic culture Lactobacillus acidophilus La-5 to produce conjugated linoleic acid (CLA), which is a potent anti-carcinogenic agent.
Methods and Results:  The conversion of linoleic acid to CLA was studied both by fermentation in a synthetic medium and by incubation of washed cells. Accumulation of CLA was monitored by gas chromatography analysis of the biomass and supernatants. While the fermentation conditions applied may not be optimal to observe CLA production in growing La-5 cells, the total CLA surpassed 50% of the original content in the washed cells after 48 h under both aerobic and micro-aerobic conditions. The restriction of oxygen did not increase the yield, but favoured the formation of trans, trans isomers.
Conclusions:  The capability of L. acidophilus La-5 to produce CLA is not dependant on the presence of milk fat or anaerobic conditions. Regulation of CLA production in this strain needs to be further investigated to exploit the CLA potential in fermented foods.
Significance and Impact of the study:  Knowledge gained through the conditions on the accumulation of CLA would provide further insight into the fermentation of probiotic dairy products. The capacity of the nongrowing cells to produce CLA is also of great relevance for the emerging nonfermented probiotic foods.     

In‐situ monitoring of Saccharomyces cerevisiae ITV01 bioethanol process using near‐infrared spectroscopy NIRS and chemometrics

The application feasibility of in‐situ or in‐line monitoring of S. cerevisiae ITV01 alcoholic fermentation process, employing Near‐Infrared Spectroscopy (NIRS) and Chemometrics, was investigated. During the process in a bioreactor, in the complex analytical matrix, biomass, glucose, ethanol and glycerol determinations were performed by a transflection fiber optic probe immersed in the culture broth and connected to a Near‐Infrared (NIR) process analyzer. The NIR spectra recorded between 800 and 2,200 nm were pretreated using Savitzky‐Golay smoothing and second derivative in order to perform a partial least squares regression (PLSR) and generate the calibration models. These calibration models were tested by external validation and then used to predict concentrations in batch alcoholic fermentations. The standard errors of calibration (SEC) for biomass, ethanol, glucose and glycerol were 0.212, 0.287, 0.532, and 0.296 g/L and standard errors of prediction (SEP) were 0.323, 0.369, 0.794, and 0.507 g/L, respectively. Calibration and validation criteria were defined and evaluated in order to generate robust and reliable models for an alcoholic fermentation process matrix. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:510–517, 2016     

Effect of aeration and agitation on extractive fermentation of clavulanic acid by using aqueous two‐phase system

In this work, the effects of agitation and aeration rates on aqueous two‐phase system (ATPS)‐based extractive fermentation of clavulanic acid (CA) by Streptomyces variabilis DAUFPE 3060 were investigated through a 2² full factorial design, where oxygen transfer rate (OTR) and oxygen uptake rate (OUR) were selected as the responses. Aeration rates significantly influenced cell growth, OUR, and CA yield, while OTR was practically the same in all the runs. Under the intermediate agitation (950 rpm) and aeration conditions (3.5 vvm) of the central point runs, it was achieved OTR of 1.617 ± 0.049 mmol L^?1 h^?1, OUR of 0.132 ± 0.030 mmol L^?1 h^?1, maximum CA production of 434 ± 4 mg L^?1, oxygen mass transfer coefficient of 33.40 ± 2.01 s^?1, partition coefficient of 66.5 ± 1.5, CA yield in the top and bottom phases of 75% ± 2% and 19% ± 1%, respectively, mass balance of 95% ± 4% and purification factor of 3.8 ± 0.1. These results not only confirmed the paramount role of O₂ supply, broth composition and operational conditions in CA ATPS‐extractive fermentation, but also demonstrated the possibility of effectively using this technology as a cheap tool to simultaneously produce and recover CA. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:1444–1452, 2016     

d‐lactic acid production from renewable lignocellulosic biomass via genetically modified Lactobacillus plantarum

d ‐lactic acid is of great interest because of increasing demand for biobased poly‐lactic acid (PLA). Blending poly‐l ‐lactic acid with poly‐d ‐lactic acid greatly improves PLA's mechanical and physical properties. Corn stover and sorghum stalks treated with 1% sodium hydroxide were investigated as possible substrates for d ‐lactic acid production by both sequential saccharification and fermentation and simultaneous saccharification and cofermentation (SSCF). A commercial cellulase (Cellic CTec2) was used for hydrolysis of lignocellulosic biomass and an l ‐lactate‐deficient mutant strain Lactobacillus plantarum NCIMB 8826 ldhL1 and its derivative harboring a xylose assimilation plasmid (ΔldhL1‐pCU‐PxylAB) were used for fermentation. The SSCF process demonstrated the advantage of avoiding feedback inhibition of released sugars from lignocellulosic biomass, thus significantly improving d ‐lactic acid yield and productivity. d ‐lactic acid (27.3 g L^?1) and productivity (0.75 g L^?1 h^?1) was obtained from corn stover and d ‐lactic acid (22.0 g L^?1) and productivity (0.65 g L^?1 h^?1) was obtained from sorghum stalks using ΔldhL1‐pCU‐PxylAB via the SSCF process. The recombinant strain produced a higher concentration of d ‐lactic acid than the mutant strain by using the xylose present in lignocellulosic biomass. Our findings demonstrate the potential of using renewable lignocellulosic biomass as an alternative to conventional feedstocks with metabolically engineered lactic acid bacteria to produce d ‐lactic acid. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:271–278, 2016     

A kinetic study on the Novozyme 435‐catalyzed esterification of free fatty acids with octanol to produce octyl esters

Octyl esters can serve as an important class of biolubricant components replacing their mineral oil counterparts. The purpose of the current work was to investigate the enzymatic esterification reaction of free fatty acids (FFA, from waste cooking oil) with octanol in a solvent‐free system using a commercial lipase Novozyme 435. It was found that the esterificaton reaction followed the Ping‐pong bi‐bi kinetics with no inhibition by substrates or products within the studied concentration range. The maximum reaction rate was estimated to be 0.041 mol L^?1 g^?1 h^?1. Additionally, the stability of Novozyme 435 in the current reaction system was studied by determining its activity and final conversion of FFA to esters after 12 successive utilizations. Novozyme 435 exhibited almost 100% enzyme activity up to 7 cycles of reaction and gradually decreased (by 5%) thereafter. The kinetic parameters evaluated from the study shall assist in the design of reactors for large‐scale production of octyl esters from a cheap biomass source. The enzyme reusability data can further facilitate mass production by curtailing the cost of expensive enzyme consumption. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:1494–1499, 2015     

Bio‐based extraction and stabilization of anthocyanins

This work reports a novel method of recovering anthocyanin compounds from highly‐pigmented grapes via a fermentation based approach. It was hypothesized that batch growth of Zymomonas mobilis on simple medium would produce both ethanol and enzymes/biomass‐acting materials, the combination of which will provide a superior extraction when compared to simple alcohol extraction. To examine this hypothesis, Z. mobilis was fermented in a batch consisting of mashed Vitis vinifera and glucose, and the recovered anthocyanin pool was compared to that recovered via extraction with ethanol. Data indicated higher amounts of anthocyanins were recovered when compared to simple solvent addition. Additionally, the percent polymeric form of the anthocyanins could be manipulated by the level of aeration maintained in the fermentation. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:601–605, 2016     

Examining the role of particle size on ammonia‐based bioprocessing of maize stover

The role of particle size in carbohydrate fractionation upon pretreatment and glucan yields upon enzymatic hydrolysis was investigated at two different temperatures, to examine the possibility of pretreating under milder conditions smaller particles, in order to satisfy pilot‐scale operational constraints. Maize stover was knife‐milled through 1‐mm and 0.5‐mm screens and pretreated by soaking in aqueous ammonia pretreatment at 60 or 110°C for 6 h. Pretreated solids were analyzed for composition and a material balance calculated for glucan, xylan, and lignin. At 60°C, milling resulted in greater delignification compared to unmilled biomass. Delignification was more uniform at 110°C. Pretreated solids were washed and cellulase hydrolysis carried out at 10% w/w solids loading, with low and high enzyme loadings. Liquid samples were drawn and concentration data developed through HPLC to calculate 48‐h glucan and xylan hydrolytic yields. The differences in hydrolytic yield between milled and unmilled treatments were found to vary with pretreatment temperature and enzyme loading. The results show that while particle size impacts carbohydrate recovery and hydrolytic yield, it is less important in bioprocessing than pretreatment temperature and enzyme loading, possibly owing to the particles’ morphology rather than the size. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 32:134–140, 2016     

An In‐situ glucose‐stimulated insulin secretion assay under perfusion bioreactor conditions

Perfusion bioreactors, unlike traditional in vitro cell culture systems, offer stringent control of physiological parameters such as pH, flow, temperature, and dissolved oxygen concentration which have been shown to have an impact on cellular behaviour and viability. Due to the relative infancy and the growing interest in these in vitro culture systems, detection methods to monitor cell function under dynamic perfusion bioreactor conditions remains one of the main challenges. In this study, INS‐1 cells, a cell line which exhibit glucose‐stimulated insulin secretion, were embedded in fibrin and cultured under perfusion bioreactor conditions for 48 h and then exposed to either a high‐, or low‐glucose concentration for 24 h. These cultures were compared to non‐bioreacted controls. Bioreacted cultures exposed to a high‐glucose concentration showed the highest glucose‐stimulated insulin secretion when compared to those in a low‐glucose environment. The stimulation index, a marker for insulin secretion functionality, increased over time. A lower incidence of apoptotic cells was observed in the bioreacted cultures when compared to non‐bioreacted ones, as evaluated by a TUNEL assay. Immunofluorescence staining of Ki67 and insulin was performed and showed no differences in the incidence of proliferative cells between conditions (bioreacted and non‐bioreacted), where all cells stained positive for insulin. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 33:454–462, 2017     

茴香酸产生菌发酵条件的优化

为提高微生物降解反式茴脑获得茴香酸的产量,对假单胞菌Pseudomonas sp.NT2的发酵参数进行优化,以提高降解过程的转化率。利用单因素试验考察碳氮源种类及浓度、反式茴脑添加量、发酵温度、接种量、初始pH以及装液量对茴香酸生成量、反式茴脑降解率的影响,通过Plackett-Burman试验和最陡爬坡试验确定影响茴香酸生成量的显著因素并获取中心点,最后采用Box-Behnken模型进行响应面优化得到最佳发酵条件并验证。结果表明氯化铵浓度、初始pH和装液量是显著影响因素,最佳发酵条件为:柠檬酸钠10 g/L,氯化铵1.26 g/L,反式茴脑添加量1%,发酵温度30℃,接种量4%,初始pH 7.9,装液量42 mL/250 mL。优化后茴香酸生成量为7.24 g/L,为优化前的3.5倍,茴香酸摩尔生成率为80.72%,反式茴脑降解率为89.81%,分别比优化前提高了270.28%和97.78%。综上,假单胞菌NT2是生物转化生产茴香酸的潜力菌株。响应面优化可以显著提高反式茴脑的降解率和茴香酸产量,这为大规模生产茴香酸奠定了基础。     

Use of biodiesel‐derived crude glycerol for vancomycin production by Amycolatopsis orientalis XMU‐VS01

Crude glycerol is a primary by‐product in the biodiesel industry. Microbial fermentation on crude glycerol for producing value‐added products provides opportunities to utilize a large quantity of this by‐product. This study investigates the potential of using the crude glycerol to produce vancomycin (glycopeptide antibiotics) through fermentation of Amycolatopsis orientalis XMU‐VS01. The results show that crude glycerol was the most effective carbon source for mycelium growth and vancomycin production, with 40–60 g/L glycerol concentration as optimal range. Among other culture medium components, potato protein (nitrogen source) and the phosphate concentration had significant effects (p<0.05) for vancomycin production. A Box‐Behnken design and response surface methodology were employed to formulate the optimal medium. Their optimal values were determined as 52.73 g/L of glycerol, 17.36 g/L of potato protein, and 0.1 g/L of dipotassium phosphate. A highest vancomycin yield of 7.61 g/L with biomass concentration of 15.8 g/L was obtained after 120 h flask fermentation. The yield of vancomycin was 3.5 times higher than with basic medium. The results suggest that biodiesel‐derived crude glycerol is a promising feedstock for production of vancomycin from A. orientalis culture.     

An approach for the improved immobilization of penicillin G acylase onto macroporous poly(glycidyl methacrylate‐co‐ethylene glycol dimethacrylate) as a potential industrial biocatalyst

The use of penicillin G acylase (PGA) covalently linked to insoluble carrier is expected to produce major advances in pharmaceutical processing industry and the enzyme stability enhancement is still a significant challenge. The objective of this study was to improve catalytic performance of the covalently immobilized PGA on a potential industrial carrier, macroporous poly(glycidyl methacrylate‐co‐ethylene glycol dimethacrylate) [poly(GMA‐co‐EGDMA)], by optimizing the copolymerization process and the enzyme attachment procedure. This synthetic copolymer could be a very promising alternative for the development of low‐cost, easy‐to‐prepare, and stable biocatalyst compared to expensive commercially available epoxy carriers such as Eupergit or Sepabeads. The PGA immobilized on poly(GMA‐co‐EGDMA) in the shape of microbeads obtained by suspension copolymerization appeared to have higher activity yield compared to copolymerization in a cast. Optimal conditions for the immobilization of PGA on poly(GMA‐co‐EGDMA) microbeads were 1 mg/mL of PGA in 0.75 mol/L phosphate buffer pH 6.0 at 25°C for 24 h, leading to the active biocatalyst with the specific activity of 252.7 U/g dry beads. Chemical amination of the immobilized PGA could contribute to the enhanced stability of the biocatalyst by inducing secondary interactions between the enzyme and the carrier, ensuring multipoint attachment. The best balance between the activity yield (51.5%), enzyme loading (25.6 mg/g), and stability (stabilization factor 22.2) was achieved for the partially modified PGA. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 32:43–53, 2016     

Composition of sugarcane waxes in rum factory wastes

Wastes produced during fermentation and distillation of crude sugarcane juice in rum factories were evaluated as a new source of waxes. The chemical composition of the crude wax extracted from adsorbat of the wastes on fuller's earth was studied by GC-mass spectrometry. Series of linear alkanes (C19-C33), and wax esters constitute the main components. In addition, phytosterols, triterpene methyl ethers, ethyl and methyl esters of fatty acids, and free fatty acids were found as minor components. Acid (predominance of C16 and C18) and alcohol portions (C26-C32) of the wax esters were analysed after saponification.     

Ultra‐stable phosphoglucose isomerase through immobilization of cellulose‐binding module‐tagged thermophilic enzyme on low‐cost high‐capacity cellulosic adsorbent

One‐step enzyme purification and immobilization were developed based on simple adsorption of a family 3 cellulose‐binding module (CBM)‐tagged protein on the external surface of high‐capacity regenerated amorphous cellulose (RAC). An open reading frame (ORF) Cthe0217 encoding a putative phosphoglucose isomerase (PGI, EC 5.3.1.9) from a thermophilic bacterium Clostridium thermocellum was cloned and the recombinant proteins with or without CBM were over‐expressed in Escherichia coli. The rate constant (k_cat) and Michaelis–Menten constant (K_m) of CBM‐free PGI at 60°C were 2,765 s^?1 and 2.89 mM, respectively. PGI was stable at a high protein concentration of 0.1 g/L but deactivated rapidly at low concentrations. Immobilized CBM (iCBM)‐PGI on RAC was extremely stable at ～60°C, nearly independent of its mass concentration in bulk solution, because its local concentration on the solid support was constant. iCBM‐PGI at a low concentration of 0.001 g/L had a half‐life time of 190 h, approximately 80‐fold of that of free PGI. Total turn‐over number of iCBM‐PGI was as high as 1.1 × 10⁹ mole of product per mole of enzyme at 60°C. These results suggest that a combination of low‐cost enzyme immobilization and thermoenzyme led to an ultra‐stable enzyme building block suitable for cell‐free synthetic pathway biotransformation that can implement complicated biochemical reactions in vitro. © 2011 American Institute of Chemical Engineers Biotechnol. Prog., 2011.     

Coupled biosynthesis and esterification of 1,2,4‐butanetriol to simplify its separation from fermentation broth

1,2,4‐Butanetriol (BT) is a valuable chemical with versatile applications in many fields and can be produced through biosynthetic pathways. As a trihydric alcohol, BT possesses good water solubility and is very difficult to separate from fermentation broth, which does complicate the production process and increase the cost. To develop a novel method for BT separation, a biosynthetic pathway for 1,2,4‐butanetriol esters with poor water solubility was constructed. Wax ester synthase/acyl‐coenzyme A: diacylglycerol acyltransferase (Atf) from Acinetobacter baylyi, Mycobacterium smegmatis, and Escherichia coli were screened, and the acyltransferase from A. baylyi (AtfA) was found to have higher capability. The BT producing strain with AtfA overexpression produced 49.5 mg/L BT oleate in flask cultivation. Through enhancement of acyl‐CoA production by overexpression of the acyl‐CoA synthetase gene fadD and deleting the acyl coenzyme A dehydrogenase gene fadE, the production was improved to 64.4 mg/L. Under fed‐batch fermentation, the resulting strain produced up to 1.1 g/L BT oleate. This is the first time showed that engineered E. coli strains can successfully produce BT esters from xylose and free fatty acids.     

Characterization of cross‐linked immobilized arylesterase from Gluconobacter oxydans 621H with activity toward cephalosporin C and 7‐aminocephalosporanic acid

Cross‐linked enzyme aggregates (CLEAs) were prepared from several precipitant agents using glutaraldehyde as a cross‐linking agent with and without BSA, finally choosing a 40% saturation of ammonium sulfate and 25 mM of glutaraldehyde. The CLEAs obtained under optimum conditions were biochemically characterized. The immobilized enzyme showed higher thermal activity and a broader range of pH and organic solvent tolerance than the free enzyme. Arylesterase from Gluconobacter oxydans showed activity toward cephalosporin C and 7‐aminocephalosporanic acid. The CLEAs had a Kcat/K_M of 0.9 M^?1/S^?1 for 7‐ACA (7‐aminocephalosporanic acid) and 0.1 M^?1/S^?1 for CPC (cephalosporin c), whereas free enzyme did not show a typical Michaelis–Menten kinetics. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 32:36–42, 2016     

Adsorption performance of creatinine on dialdehyde nanofibrillated cellulose derived from potato residues

Potato residue is vastly produced in the food industry but it is landfilled. This article describes the treatment of purified cellulose derived from potato residues by a high pressure homogenizer to produce nano‐fibrillated cellulose (NFC), which was then oxidized by sodium periodate to prepare dialdehyde nano‐fibrillated cellulose (DANFC). The produced NFC and DANFC were characterized by a scanning electron microscope (SEM) and Fourier transform infrared spectroscopy (FTIR). The orthogonal experiment was induced to obtain the maximum degree of oxidation (DO) on DANFC. The results indicated that the optimal conditions were 40°C and pH 3. Alternatively, the isotherm and kinetic studies for the adsorption of creatinine on DANFC with different DOs (70.5 and 88.8%) were investigated, and the experimental results fitted well into Freundlich isotherm model and pseudo second‐order kinetic model. The maximum adsorption capacities of DANFCs with the DO of 70.55 and 88.85% were 6.7 and 17.2 mg g^?1, respectively, which were achieved under the conditions of 37°C and initial creatinine concentration of 100 mg L^?1. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 32:208–214, 2016     

Improved assembly of bispecific antibodies from knob and hole half‐antibodies

A process was developed for large‐scale assembly of IgG₁ and IgG₄ bispecific antibodies from knob and hole half‐antibodies. We optimized assembly conditions such as pH, temperature, stabilizers, and reducing agent. We also identified and exploited structural changes unique to knob and hole half‐antibodies with the result of improving assembly outcome, specifically storing half‐antibodies at higher pH will condition them to assemble more rapidly and produce fewer high molecular‐weight species (HMWS). Application of heat to the assemblies resulted in an acceleration of assembly rate, with optimal formation of bispecific achieved at 37°C. IgG₄ half‐antibodies were unusually sensitive to temperature‐dependent formation of HMWS in pre‐assembly conditioning as well as during assembly. We selected l ‐histidine and Polyvinylpyrrolidone (PVP) as stabilizers to prevent HMWS formation in IgG₄, and achieved rapid and high‐efficiency assemblies. Using optimized assembly conditions, we developed and scaled up a method for assembling bispecific antibody with 90% assembly efficiency over 6 h with minimal impact to product quality, generating a pool with bispecific antibody for downstream processing. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:1315–1322, 2015