Dynamics of recombinant protein production by mammalian cells in immobilized perfusion culture

In spite of the generally stable nature of immobilized perfusion culture, its profile of target protein production frequently shows variations. This might be explained by the drift in the metabolism of cultured cells. To address this issue, we performed a set of four Opticell bioreactor cultures producing recombinant anticogulant protein PCGFX. All the cultures lasted 40-50 days with the oxygen consumption rate (OCR) mostly around 10 μmol min⁻¹; nevertheless, glucose and lactate metabolism was fluctuated with a parallel fluctuation in the recombinant protein productivity (RPP). The mean productivity of recombinant PCGFX was determined to be about 1.0 mg day⁻¹ for all the cultures. The statistical analysis revealed a significant correlation between the lactate production rate (LPR) and RPP in two cultures. A significant correlation was further found between average OCR and RPP in another culture where OCR was exceptionally lowered under serum-free conditions. No parameter significantly correlated with RPP in the remaining one culture; thus, the overt drift of RPP resulted, at least partly, from that of the cell metabolic activity and the present data should be helpful to explore a strategy for maximizing productivity.     

Bioreactor operation for transgenic Nicotiana tabacum cell cultures and continuous production of recombinant human granulocyte-macrophage colony-stimulating factor by perfusion culture

The production of hGM-CSF was investigated in both a flask and a 5-l bioreactor, using transgenic Nicotiana tabacum suspension cells. While the maximum cell density and secreted hGM-CSF in the flask were 15.4 g l⁻¹ and 6.5 μg l⁻¹, respectively, those in the bioreactor were 15.6 g l⁻¹ and 7.6 μg l⁻¹. No detectable growth inhibition, shorter production of hGM-CSF and reduced cell viability in the batch bioreactor were observed under the specific conditions used compared with the flask culture. To improve the productivity, a perfusion culture was carried out in the bioreactor, with three different perfusion rates (0.5, 1.0 and 2.0 day⁻¹). In all cases, the hGM-CSF in the medium was significantly increased during the overall culture period (16 days), with maximum values 3.0-, 9.4- and 6.0-fold higher than those obtained in the batch cultures, respectively, even though the intracellular hGM-CSF content was not significantly varied by the perfusion rate. In terms of the total amount of hGM-CSF secreted, 205.5, 1073.2 and 1246.3 μg accumulated in the perfusate within 16 days at the perfusion rates of 0.5, 1.0 and 2.0 day⁻¹, respectively. It was concluded that the beneficial effect of perfusion on the production of hGM-CSF originated from the reduced proteolytic degradation due to the lower protease activity caused by the perfusion. Additionally, the cell growth and physiology in the perfusion culture were somewhat negatively affected by the increased perfusion rate, although the dry cell density steadily increased, and as a result, 19.4, 22.4 and 22.9 g l⁻¹ of maximum cells were obtained with perfusion rates of 0.5, 1.0 and 2.0 day⁻¹, respectively. This work highlighted the importance of proteolytic degradation in plant cell cultures for the production of secretory proteins and the feasibility of perfusion strategies for the continuous production of foreign proteins by the prevention of protein loss due to proteolytic enzymes.     

Kinetics and modeling of GM-CSF production by recombinant yeast in a three-phase fluidized bed bioreactor

Continuous production of a recombinant murine granulocyte-macrophage colony-stimulating factor (GM-CSF) by Saccharomyces cerevisiae strain XV2181 (a/a, Trp 1) containing plasmid palphaADH2 and immobilized on porous glass beads in a fluidized bed bioreactor was studied. Kinetic models for plasmid stability, cell growth, and protein production in the three-phase fluidized bed bioreactor were developed and used to study the effects of solid loading or cell immobilization on plasmid stability and recombinant protein production. With increasing cell immobilization or solid loading in the bioreactor, plasmid stability and protein production improved significantly. The improvements could be attributed to the decreased theta value, which is the plasmid loss probability during cell division and is an indication of segregational instability of the recombinant cell, and the increased alpha value, which is the ratio of the specific growth rate of a plasmid-carrying cell to that of a plasmid-free cell and is indicative of competitive stability of the recombinant cell culture. theta decreased from 0.552 to 0.042 and alpha increased from 0.351 to 0.991 when solid loading in the bioreactor was increased from 5% (v/v) to 33%. The model simulation also showed that the specific growth rate of cells in the bioreactor was lower at higher solid loading. This indicated that there was significant mass transfer limitation, particularly for oxygen transfer, when the total cell density in the bioreactor was high at high solid loading. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 470-477, 1997.     

Purification and characterization of a chitosanase from Serratia marcescens TKU011

A chitosanase was purified from the culture supernatant of Serratia marcescens TKU011 with shrimp shell wastes as the sole carbon/nitrogen source. Zymogram analysis revealed the presence of chitosanolytic activity corresponding to one protein, which was purified by a combination of ion-exchange and gel-filtration chromatography. The molecular weight of the chitosanase was 21 kDa and 18 kDa estimated by SDS–PAGE and gel-filtration, respectively. The optimum pH, optimum temperature, pH stability, and thermal stability of the chitosanase were 5, 50 °C, pH 4–8, and <50 °C, respectively. The chitosanase was inhibited completely by EDTA, Mn²⁺, and Fe²⁺. The results of peptide mass mapping showed that three tryptic peptides of the chitosanase were identical to a chitin-binding protein Cbp21 from S. marcescens (GenBank accession number gi58177632) with 63% sequence coverage.     

Cloning of the nitrile hydratase gene from Nocardia sp. in Escherichia coli and Pichia pastoris and its functional expression using site-directed mutagenesis

To obtain a recombinant Rhodococcus or Nocardia with not only higher enzymatic activity but also better operational stability and product-tolerance ability for bioconversion of acrylamide from acrylonitrile, an active and stable expression system of nitrile hydratase (NHase) was tried to construct as the technical platform of genetic manipulations. Two NHase genes, NHBA and NHBAX, from Nocardia YS-2002 were successfully cloned, based on bioinformatics design of PCR primers, and inserted into plasmid pUC18 and pET32a, respectively. Then, two recombinant Escherichia coli strains, JM105 (pUC18-NHBA) and BL21 (DE3) (pET32a-NHBAX) were constructed and their expressions of NHase were focused. The induction results showed that there was either no NHase activity in JM105 (pUC18-NHBA), or as low as 0.04 U (1 U=1 μmol acrylamide min⁻¹ mg⁻¹ dry cell) in BL21 (DE3) (pET32a-NHBAX). SDS-PAGE results showed that the -subunit of NHBA and NHBAX could not be efficiently expressed in both recombinant E. coli strains. The novel Pichia pastoris system was also applied to express NHase, but the expression level remained quite low (0.5–0.6 U) and the protein was unstable. For solving this problem, a possible genetic strategy, site-directed mutagenesis of the -subunit of the NHase was carried out. After the successful mutagenesis of the original rare start codon gtg into atg, a new recombinant strain, E. coli XL1-Blue (pUC18-NHBA^M), was screened and the NHase activity stably reached as high as 51 U under the same induction conditions.     

Hydrolysis of lactose in whey permeate by immobilized β-galactosidase from Kluyveromyces fragilis

Neutral β-galactosidase from Kluyveromyces fragilis was immobilized on silanized porous glass modified by glutaraldehyde binding, with retention of more than 90% of its activity. Marked shifts in optimum pH (from 7.0 to 6.0) and temperature (from 35°C to 50°C) of the solid-phase enzyme were observed together with high catalytic activity and reasonable stability at wider pH and temperature ranges than those of the free enzyme. Highly efficient lactose saccharification (86–90%) in whey permeate was achieved both in a batch process and in a recycling packed-bed bioreactor.     

Synthesis, radiolabeling and receptor binding of [3H][(1S,2R)ACPC2]endomorphin-2

Previously, we have shown that substitution of Pro² for cis-2-aminocyclopentanecarboxylic acid, ACPC in endomorphin-2 results in an analogue with greatly augmented proteolytic stability, high μ-opioid receptor affinity and selectivity. We now report the synthesis and biochemical characterization of [³H][(1S,2R)ACPC²]endomorphin-2 with a specific activity of 1.41 TBq/mmol (38.17 Ci/mmol). Specific binding of [³H][(1S,2R)ACPC²]endomorphin-2 was saturable and of high affinity with an equilibrium dissociation constant, K_d = 1.80 ± 0.21 nM and receptor density, B_max = 345 ± 27 fmol × mg protein⁻¹ at 25 °C in rat brain membranes. Similar affinity values were obtained in kinetic and displacement assays. Both Na⁺ and Gpp(NH)p decreased the affinity proving the agonist character of the radioligand. [³H][(1S,2R)ACPC²]endomorphin-2 retained the μ-specificity of the parent peptide. The new radioligand will be a useful tool to map the topographical requirements of μ-opioid peptide binding due to its high affinity, selectivity and enzymatic stability.     

High cell density cultivation of <Emphasis Type="Italic">Escherichia coli</Emphasis> with surface anchored transglucosidase for use as whole-cell biocatalyst for α-arbutin synthesis

A fed-batch culture strategy for the production of recombinant Escherichia coli cells anchoring surface-displayed transglucosidase for use as a whole-cell biocatalyst for α-arbutin synthesis was developed. Lactose was used as an inducer of the recombinant protein. In fed-batch cultures, dissolved oxygen was used as the feed indicator for glucose, thus accumulation of glucose and acetate that affected the cell growth and recombinant protein production was avoided. Fed-batch fermentation with lactose induction yielded a biomass of 18 g/L, and the cells possessed very high transglucosylation activity. In the synthesis of α-arbutin by hydroquinone glucosylation, the whole-cell biocatalysts showed a specific activity of 501 nkat/g cell and produced 21 g/L of arbutin, which corresponded to 76% molar conversion. A sixfold increased productivity of whole cell biocatalysts was obtained in the fed-batch culture with lactose induction, as compared to batch culture induced by IPTG.     

Production of antifungal recombinant peptides in Escherichia coli

Antifungal peptides derived from the human bactericidal/permeability-increasing protein (BPI) were produced in Escherichia coli as fusion proteins with human BoneD. Bacterial cultures transformed with the gene encoding the fusion protein were grown to a high cell density (OD(600)>100), and induced with L-arabinose to initiate product expression. Fusion protein accumulated into cytoplasmic inclusion bodies and recombinant peptide was released from BoneD by acid hydrolysis at an engineered aspartyl-prolyl dipeptide linker. Acid hydrolysis of purified inclusion bodies at pH <2.6 followed Arrhenius kinetics and did not require prior inclusion body solubilization in detergents or denaturants. Surprisingly, at pH <2.6 and 85 degrees C, cell lysis and aspartyl-prolyl hydrolysis with concomitant peptide release occurred simultaneously. Bacterial cultures were, therefore, adjusted to approximately pH 2.6 with HCl directly in the bioreactor and incubated at elevated temperature. Peptide, which is soluble in the aqueous acidic environment, was separated from the insoluble material and purified using column separation techniques. Recombinant peptide was separated from the hydrolyzed bioreactor culture with >76% recovery and a final peptide purity of >97%. Antifungal peptide prepared by recombinant and solid phase synthesis methods demonstrated similar activity against Candida sp. in a broth microdilution assay.     

Emulsion-stabilizing properties of chitosan in the presence of whey protein isolate: Effect of the mixture ratio, ionic strength and pH

The emulsion-stabilizing properties of a chitosan preparation were compared as a function of the whey protein isolate/chitosan mixture ratio (WPI/CNI) and the ionic strength (μ), at pH 5.5 and 6.0. At both pH conditions, general decreases in emulsion stability towards charge neutralization flocculation and syneresis were observed at WPI/CNI > 5. This was particularly evident at pH 6.0, due to a lower surface net charge (lower electrostatic stabilization). In counterpart, when μ was increased, the higher load of chitosan at pH 6.0 produced higher stabilities (higher steric stabilization), in spite of comparable decreases of surface net charge at both pH conditions. The transition from soluble to insoluble protein–chitosan complex formation in mixtures at pH 6.0 and WPI/CNI > 5.0 was due to an emulsion destabilization towards syneresis, whereas soluble complex formation at pH 5.5 also produced syneresis. It showed that soluble protein–chitosan adsorbing complex formation prior homogenization is not essentially linked to emulsion stabilization.     

Air pressure effects on biomass yield of two different Kluyveromyces strains

The use of air pressure as a way of improving oxygen transfer in aerobic bioreactors was investigated. To compare the air pressure effects with traditional air bubbled cultures, experiments using a pressure reactor and a stirred flask, with the same oxygen transfer rate, were made. Kluyveromyces marxianus is an important industrial yeast and some of it show a “Kluyver effect” for lactose: even under oxygen limited growth conditions, certain disaccharides that support aerobic, respiratory growth, are not fermented. This study deals with the effect of increased pressure on the physiological behavior of two Kluyveromyces strains: K. marxianus ATCC10022 is a lactose-fermenting strain, whereas K. marxianus CBS 7894 has a Kluyver-effect for lactose. For K. marxianus ATCC10022 an air pressure increase of 2 bar led to a 3-fold increase in biomass yield. When air pressure increased an enhancement of ethanol oxidation of cell yeasts was also observed. Batch cultures of K. marxianus CBS 7894 exhibited different growth behaviour. Its metabolism was always oxidative and ethanol was never produced. With the increase in air pressure, it was possible to increase the productivity in biomass of K. marxianus CBS 7894. As a response to high oxygen concentrations, due to the increase in oxygen partial pressure, oxidative stress in the cells was also studied. Antioxidant defences, such as superoxide dismutase, catalase, and glutathione reductase, were at high activity levels, suggesting that these yeast strains could tolerate the increased pressures applied.     

Purification and activation of a recombinant histidine-tagged pro-transglutaminase after soluble expression in Escherichia coli and partial characterization of the active enzyme

Pro-transglutaminase from Streptomyces mobaraensis was expressed in Escherichia coli as a fusion protein carrying a C-terminal histidine tag (pro-MTG-His₆). The recombinant organism was cultivated in 15 L bioreactor scale and pro-MTG-His₆ was purified by immobilized metal affinity chromatography. Activation of the inactive pro-enzyme using trypsin resulted in an unexpected degradation of the transglutaminase and a concomitant loss of activity. Therefore, a set of commercially available proteases was investigated for their activation potential without destroying the target enzyme. Besides trypsin, chymotrypsin and proteinase K were found to activate but hydrolyze the (pro-MTG-His₆). Cathepsin B, dispase I, and thrombin were shown to specifically hydrolyze pro-MTG-His₆ without deactivation. TAMEP, the endogeneous protease from S. mobaraensis was purified for comparison and also found to activate the recombinant histidine-tagged transglutaminase without degradation. The TAMEP activated MTG-His₆ was purified and characterized. The specific activity (23 U/mg) of the recombinant histidine-tagged transglutaminase, the temperature optimum (50 °C), and the temperature stability (t_1/2 at 60 °C = 1.7 min) were comparable to the wild-type enzyme. A C-terminal peptide tag did neither affect the activity nor the stability but facilitated the purification. The purification of the histidine-tagged protein is possible before or after activation.     

Stability of plasmid and expression of a recombinant gonadotropin-releasing hormone (GnRH) vaccine in Escherichia coli

In our previous studies, the recombinant gonadotropin-releasing hormone (GnRH) peptide was constructed into a T7 RNA polymerase-based expression system. The recombinant gene encoding GnRH3-hinge-MVP, which contained three repeated GnRH units, a fragment of hinge region (225-232/225′-232′), and a T cell epitope of measles virus protein, was cloned into Escherichia coli BL21 harboring pED-GnRH3. The high activity of T7 RNA polymerase could make the expression system very powerful for high-level expression of the recombinant protein. However, during the large-scale production of recombinant protein, the productivity of the fermentation process was directly affected by many factors, such as plasmid stability, protein production, and culture conditions. In this study, we studied the effects of various culture conditions on the plasmid stability and the target protein yield including selective pressure, the time of induction by lactose, and the number of successive cultures. The results indicate that the plasmid instability may be caused by a loss of plasmid rather than structural change. However, to go down to future generations, engineered bacteria have the stability of plasmid and protein yield to a large extent. The amount of the fusion protein was also up to 40% of the total cell protein after the 50th generation. These data would be useful for the industrial production of the recombinant GnRH vaccine.This work was supported by the National High Technology “863” Programs of China (no. 2002 AA217031-2), a Grant-in-Aid from China National Natural Science Fund Committee (grant no. 30270298) and Jiangsu Natural Science Fund Committee (grant no. BK 95092309 and BG2001011).     

Purification and characterization of an enantioselective carbonyl reductase from Candida viswanathii MTCC 5158

A highly enantioselective carbonyl reductase produced by a new yeast strain Candida viswanathii MTCC 5158, which was isolated using an acetophenone enriched medium, has been purified and characterized. The enzyme has been purified to near homogeneity using ammonium sulfate precipitation, ion exchange and gel filtration chromatography. The molecular properties of the carbonyl reductase suggested the native enzyme to be tetrameric, with an apparent molecular weight of 120 kDa, the monomer being about 29 kDa. Acetyl aryl ketones were found to be the preferred substrates for the enzyme and the best reaction was the enantioselective reduction of acetophenone. The enzyme yielded (S)-alcohol in preference to (R)-alcohol and utilized NADH, but not NADPH as the cofactor. The purified enzyme exhibited maximum enzyme activity at pH 7.0 and 60 °C. The enzyme retained about 80% of its activity after 7 h incubation at 25 °C in sodium phosphate buffer (50 mM, pH 7.0). The addition of reducing agents like dithiothreitol and β-mercaptoethanol enhanced the enzyme activity while organic solvents, detergents and chaotropic agents had deleterious effect on enzyme activity. Metal chelating agents like hydroxyquinoline and o-phenanthroline have significant effect on enzyme activity suggesting that the carbonyl reductase required the presence of a tightly bound metal ion for activity or stability. The maximum reaction rate (V_max) and apparent Michaelis–Menten constant (K_m) for acetophenone and NADH were 59.21 μmol/(min mg) protein and 0.153 mM and 82.64 μmol/(min mg) protein and 0.157 mM at a concentration range of 0.2–2 mM acetophenone (NADH fixed at 0.5 mM) and 0.1–0.5 mM NADH (acetophenone fixed at 2 mM), respectively.     

Optimization of bio-indigo production by recombinant E. coli harboring fmo gene

A bacterial flavin-containing monooxygenase (FMO) gene was cloned from Methylophaga aminisulfidivorans MP^T, and a plasmid pBlue 2.0 was constructed to express the bacterial fmo gene in E. coli. To increase the production of bio-indigo, upstream sequence size of fmo gene was optimized and response surface methodology was used. The pBlue 1.7 plasmid (1686 bp) was prepared by the deletion of upstream sequence of pBlue 2.0. The recombinant E. coli harboring the pBlue 1.7 plasmid produced 662 mg l⁻¹ of bio-indigo in tryptophan medium after 24 h of cultivation in flask. The production of bio-indigo was optimized using a response surface methodology with a 2ⁿ central composite design. The optimal combination of media constituents for the maximum production of bio-indigo was determined as tryptophan 2.4 g l⁻¹, yeast extract 4.5 g l⁻¹ and sodium chloride 11.4 g l⁻¹. In addition, the optimum culture temperature and pH were 30 °C and pH 7.0, respectively. Under the optimized conditions mentioned above, the recombinant E. coli harboring pBlue 1.7 plasmid produced 920 mg of bio-indigo per liter in optimum tryptophan medium after 24 h of cultivation in fermentor. The combination of truncated insert sizes and culture optimization resulted in a 575% increase in the production of bio-indigo.     

Enhancement of growth and gymnodimine production by the marine dinoflagellate, Karenia selliformis

Because of its novel bioactive properties the production of gymnodimine for use as a pharmaceutical precursor has aroused interest. The dinoflagellate, Karenia selliformis produces gymnodimine when grown in bulk culture using GP + selenium medium but the growth rates (μ) and levels of gymnodimine are low (μ, 0.05 days⁻¹; gymnodimine 250 μg L⁻¹ max). We describe the effects of organic acid additions (acetate, glycolate, alanine and glutamate additions and combinations of these) in enhancing growth and gymnodimine production in axenic cultures. The most effective organic acid combinations in decreasing order were: glycolate/alanine > acetate > glycolate. Glycolate/alanine optimised gymnodimine production by prolonging growth (maximum cell yield, 1.76 × 10⁵ cells mL⁻¹; gymnodimine, 1260 μg L⁻¹; growth rate (μ), 0.2 days⁻¹) compared to the control (growth maximum cell yield, 7.8 × 10⁴ cells mL⁻¹; gymnodimine, 780 μg L⁻¹; μ, 0.17 days⁻¹). Acetate enhanced gymnodimine by stimulating growth rate (μ, 0.23 days⁻¹) and the large concentration of gymnodimine per cell (16 pg cell⁻¹ cf. 9.8 pg cell⁻¹ for the control) suggests a role for this compound in gymnodimine biosynthesis. Amending culture media with Mn²⁺ additions resulted in slightly decreased growth in control cultures and increased the gymnodimine while in glycolate/alanine cultures growth was stimulated but gymnodimine production decreased. The results suggest that the organic acid can enhance gymnodimine production by either enhancing growth maximum or the biosynthetic pathway.     

Recombinant expression, characterization, and pulp prebleaching property of a Phanerochaete chrysosporium endo-β-1,4-mannanase

A Phanerochaete chrysosporium cDNA predicted to encode endo-1,4-β-d-mannanase, man5D, was cloned and expressed in Aspergillus niger. The coding region of the gene man5D was predicted to contain, in order from the N-terminal: a secretory signal peptide, cellulose-binding domain, linker region, and glycosyl hydrolase family 5 catalytic site. The enzyme was purified from culture filtrate of A. niger transformants that carried the recombinant man5D. Recombinant Man5D had an apparent molecular size of about 65 kDa by SDS-PAGE, and optimal activity at pH 4.0–6.0 and 60 °C. It was stable from pH 4.0 to 8.0 and up to 60 °C. The enzyme showed affinity for Avicel cellulose, suggesting that the predicted cellulose-binding domain is biologically functional. The specific activities of Man5D on mannan, galactomannan, and glucomannan at pH 5 and 60 °C ranged from 160 to 460 μmol/(min mg), with apparent K_m values from 0.54 to 2.3 mg/mL. Product analysis results indicated that Man5D catalyzes endo-cleavage, and appears to have substantial transglycosylase activity. When used to treat softwood kraft pulp, Man5D hydrolyzed mainly glucomannan and exhibited a positive effect as a prebleaching agent. Compared to a commercial prebleaching with xylanase, the prebleaching effect of Man5D was weaker but with reduced loss of fibre yield as determined by the release of solubilized sugars.     

抗菌肽Cec4a的重组表达和抗菌活性研究*

目的:构建Cec4a的原核重组表达体系,通过诱导表达、酶切纯化获得重组蛋白,并检测产物的抗菌活性。方法:基于Cec4a的序列设计引物,克隆Cec4a基因的DNA片段。利用原核表达载体(pCold-SUMO)构建重组原核表达质粒,并将其转化到大肠杆菌C41(DE3)等感受态细胞,使用IPTG进行诱导表达。通过Ni-NTA亲和层析柱纯化,获得含有His-SUMO标签的重组Cec4a融合蛋白。在SUMO蛋白酶酶切后,再次使用Ni-NTA亲和层析纯化,得到目的蛋白,最后用鲍曼不动杆菌(ATCC19606)作为指示菌检测表达产物的抗菌活性。结果:成功构建pCold-SUMO-Cec4a原核表达质粒,测序分析其序列与预期结果一致。Cec4a融合蛋白表达量为42.8mg/L,纯化后的Cec4a重组蛋白对鲍曼不动杆菌的MIC为4 μg/mL。结论:通过原核表达,并经Ni-NTA亲和层析纯化,获得了具有抗菌活性的重组蛋白Cec4a,为研究Cec4a的生物活性、抗菌机制及应用奠定了基础。     

Effect of oxygen supply on cell growth and saponin production in bioreactor cultures of Panax ginseng

The effects of oxygen supply within the range 20.8–50% (using pure oxygen and air), on cell cultures of Panax ginseng were investigated in a balloon-type bubble bioreactor (5 L capacity, containing 4 L Murashige and Skoog medium, supplemented with 7.0 mg L⁻¹ indolebutyric acid, 0.5 mg L⁻¹ kinetin and 30 g L⁻¹ sucrose). A 40% oxygen supply was found to be optimal for the production of both cell mass and saponin yielding values of 12.8 g (DW) L⁻¹, 4.5 mg (g DW)⁻¹ on day 25, respectively. Low (20.8%, 30%) and high (50%) oxygen concentration supplies were unfavorable to cell growth and saponin accumulation. The results indicate that oxygen supplementation to bioreactor-based ginseng cultures was beneficial for biomass accumulation and saponin production.