Behaviour of vanadate and vanadium-transferrin complex on different anion-exchange columns. Application to in vivo 48V-labelled rat serum

The behaviour of free [48V]vanadate and [48V]vanadium-transferrin complex was investigated on five different anion-exchange columns (Mono Q 5/5 HR, Hitrap Q HP, Sepharose Q FF, Sepharose DEAE FF and Hitrap Q XL). The recovery of both V-compounds was quantitative. The peak shape and retention time of vanadate varied according to the type of column. The vanadium-transferrin complex also showed different elution patterns depending on the type of column. Especially in case of the Sepharose Q FF, Mono Q 5/5 HR and Hitrap Q XL columns the vanadium-transferrin binding was degraded during elution on the column. The results clearly prove that care should be taken as to the choice of column for speciation purposes of vanadium compounds in order to prevent various artefacts showing up in the chromatograms. A Hitrap Q HP column was used to fractionate different vanadium compounds in rat serum.     

Evaluation of three expanded bed adsorption anion exchange matrices with the aid of recombinant enhanced green fluorescent protein overexpressed in Escherichia coli

Three anion exchanger expanded bed adsorption (EBA) matrices: Streamline DEAE, Streamline Q XL and Q Hyper Z were evaluated with the aid of EFGP from an ultrasonic homogenate of Escherichia coli. Two pH of buffer were tested. Capture was done in an expanded mode whereas elution was done in a packed mode. The same conditions were chosen for evaluation of the three matrices. We observed a loss of EGFP (8-15%) in the through flow fraction especially with the Streamline Q XL matrix, probably due to an aggregation of beads during sample application. The beads of this matrix possess tentacles which probably retain a lot of cellular and molecular debris. The two other matrices gave a good purification of the EGFP (7-15-fold) but the Q Hyper Z matrix appeared to give the best results. It is composed of little size and density beads which lead to a higher exchange surface and then a better mass transfer.     

Matrix assisted refolding of proteins by ion exchange chromatography

Two different approaches of matrix assisted refolding have been evaluated and compared to conventional refolding by dilution. Bovine alpha-lactalbumin was used for the studies as model protein. It was adsorbed under denaturing conditions on an ion exchange matrix and refolding was completed on the column prior to elution or, depending on the buffer system, in the eluate. Agarose based chromatography matrices showed high capacities for the denatured alpha-lactalbumin. A positive effect on the yield of refolded protein by the matrix could be observed for Fractogel EMD DEAE and a negative for Toyopearl DEAE 650M, DEAE Sepharose FF and Q Sepharose FF. In the case of Fractogel EMD DEAE the ion exchange surface might act as a folding helper. This property may be caused by the grafted polymers. For Source 30Q only a marginal negative influence on the refolding kinetics was observed, thus the ion exchanger is only a mean for removal of chaotropic agents. Refolding on the column is characterized by a low yield but high productivity due to significant reduction of refolding time.     

Lumped parameter model for prediction of initial breakthrough profiles for the chromatographic capture of antibodies from a complex feedstock

A simple mathematical model to predict initial breakthrough profiles from preparative chromatographic separations of biological macromolecules has been developed. A lumped parameter approach was applied, employing Langmuirian adsorption kinetics to describe the rate of mass transfer (MT) from the bulk liquid in the column to the bound state. Equilibrium and kinetic adsorption data were determined for six different packed bed chromatographic adsorbents: two derivatised with rProtein A; and four functionalised with synthetic low molecular weight ligands. All adsorption isotherms were well described by the Langmuir model, whereas the data fitting to kinetic batch experiments showed that the model was inadequate after the first approximately 25 min of adsorption for four of the six adsorbents. The model underestimated the dynamic Ig breakthough on packed beds of rProtein A Sepharose FF, MabSelect, MBI HyperCel, and MabSorbent A1P, applying a feedstock of 20-100% (v/v) clarified rabbit antiserum. However, when employing a maximum adsorption capacity 25% greater than that determined in batch binding studies, excellent agreement was obtained at all antiserum strengths for most adsorbents. Useful insights into scale-up and process design can be obtained by applying the model, without determining tentative parameters specific for each adsorbent and target protein concentration. However, the model parameters are solvent dependent so a prerequisite for its true applicability is that binding is both Langmuirian and essentially independent of the ionic strength of the feedstock applied.     

Bioprocess considerations for expanded-bed chromatography of crude canola extract: sample preparation and adsorbent reuse

Compared to the conventional microbial and mammalian systems, transgenic plants produce proteins in a different matrix. This provides opportunities and challenges for downstream processing. In the context of the plant host Brassica napus (canola), this work addresses the bioprocessing challenges of solid fractionation, resin fouling by native plant components (e.g., oil, phenolics, etc.), hydrodynamic stability, and resin reuse for expanded bed adsorption for product capture. Plant tissue processing and subsequent protein extraction typically result in an extract with a high content of solids containing a wide particle-size distribution. Without removal of larger particles, the column inlet distributor plugged. The larger particles (> 50 microm) were easily removed through centrifugal settling comparable to that attainable with a scroll decanter. The remaining solids did not affect the column performance. Less than 4% of the lipids and phenolics in the fed extract bound to STREAMLINE trade mark DEAE resin, and this small proportion could be satisfactorily removed using recommended clean-in-place (CIP) procedures. Hydrodynamic expansion and adsorption kinetics of the STREAMLINE trade mark DEAE resin were maintained throughout 10 cycles of reuse, as was the structural integrity of the resin beads. No significant accumulation of N-rich (e.g., proteins) and C/O-rich components (e.g., oil and phenolics) occurred over the same period.     

The effect of column verticality on separation efficiency in expanded bed adsorption

The effect of column verticality on liquid dispersion and separation efficiency in expanded bed adsorption columns was investigated using 1 and 5 cm diameter columns. Column misalignment of only 0.15° resulted in the reduction of the Bodenstein number from 140 to 50 for the 1 cm dia. column and from 75 to 45 for the 5 cm dia. column. This degree of misalignment was not detectable by visual assessment of adsorbent particle movement within the column. Depending on the relative importance of transport limitations, kinetic limitations and dispersion to any specific separation, this increase in dispersion with column alignment can significantly affect separation efficiency. Pure protein breakthrough profiles resulting from the application of bovine serum albumin onto STREAMLINE Q XL demonstrated that, at 10% breakthrough, 7.8% more protein could be applied to a vertical 1 cm dia. column compared to the same column misaligned by 0.15°. When an unclarified yeast homogenate was applied to a 1 cm dia. vertical column packed with STREAMLINE DEAE, 10% breakthrough of glucose-6-phosphate dehydrogenase (G6PDH) corresponded to a load 55% greater compared to the same column aligned 0.185° off-vertical. The G6PDH breakthrough curves for vertical and 0.15° off-vertical runs performed using a 5 cm column were essentially indistinguishable.     

Minimising biomass/adsorbent interactions in expanded bed adsorption processes: a methodological design approach

Expanded bed adsorption (EBA) is an integrated technology for the primary recovery of proteins from crude feedstock. Interactions between solid matter in the feed suspension and fluidised adsorbent particles influence bed stability and therefore have a significant impact on protein adsorption in expanded beds. In order to design efficient and reliable EBA processes a strategy is needed, which allows to find operating conditions, where these adverse events do not take place. In this paper a methodological approach is presented, which allows systematic characterisation and minimisation of cell/adsorbent interactions with as little experimental effort as possible. Adsorption of BSA to the anion exchanger Streamline Q XL from a suspension containing S. cerevisiae cells was chosen as a model system with a strong affinity of the biomass towards the stationary phase. Finite bath biomass adsorption experiments were developed as an initial screening method to estimate a potential interference. The adhesiveness of S. cerevisiae to the anion exchanger could be reduced significantly by increasing the conductivity of the feedstock. A biomass pulse response method was used to find optimal operation conditions showing no cell/adsorbent interactions. A good correlation was found between the finite bath test and the pulse experiment for a variety of suspensions (intact yeast cells, E. coli homogenate and hybridoma cells) and adsorbents (Streamline Q XL, DEAE and SP), which allows to predict cell/adsorbent interactions in expanded beds just from finite bath adsorption tests. Under the optimised operating conditions obtained using the prior methods, the stability of the expanded bed was investigated during fluidisation in biomass containing feedstock (up to 15% yeast on wet weight basis) employing residence time distribution analysis and evaluation by an advanced model. Based on these studies threshold values were defined for the individual experiments, which have to be achieved in order to obtain an efficient EBA process. Breakthrough experiments were conducted to characterise the efficiency of BSA adsorption from S. cerevisiae suspensions in EBA mode under varying operating conditions. This allowed to correlate the stability of the expanded bed with its sorption efficiency and therefore could be used to verify the threshold values defined. The approach presented in this work provides a fast and simple way to minimise cell/adsorbent interactions and to define a window of operation for protein purification using EBA.     

Use of a phosphotyrosine-antibody pair as a general detection method in homogeneous time-resolved fluorescence: application to human immunodeficiency viral protease

A homogeneous time-resolved fluorescence (HTRF) assay has been developed for human immunodeficiency viral (HIV) protease. The assay utilizes a peptide substrate, differentially labeled on either side of the scissile bond, to bring two detection components, streptavidin-cross-linked XL665 (SA/XL665) and a europium cryptate (Eu(K))-labeled antiphosphotyrosine antibody, into proximity allowing fluorescence resonance energy transfer (FRET) to occur. Cleavage of the doubly labeled substrate by HIV protease precludes complex formation, thereby decreasing FRET, and allowing enzyme activity to be measured. Potential substrates were evaluated by HTRF with the best results being obtained using (LCB)K4AVSQNbeta-NapPIVpYA(NH2) and Eu(K)-pY20 where the peptide titrated with an EC50 of 7.7 +/- 0.3 nM under optimized detection conditions. Using these HTRF detection conditions, HIV protease cleaved the substrate in 50 mM NaOAc, 150 mM KF, 0.05% Tween 20, pH 5.5, with apparent first-order kinetics with a Km of 37.8 +/- 8.7 microM and a kcat of 0.95 +/- 0.07 s-1. Examination of the first-order rate constant versus enzyme concentration suggested a Kd of 9.4 +/- 2.7 nM for the HIV protease monomer-dimer equilibrium. The HTRF assay was also utilized to measure the inhibition of the enzyme by two known inhibitors.     

高效液相尺寸排阻色谱-多角度激光散射定量检测灭活禽流感病毒抗原中完整病毒颗粒

本研究旨在建立一种灭活禽流感病毒原料液中完整病毒颗粒准确定量的方法。针对直接采用高效液相尺寸排阻色谱法（high performance size exclusion chromatography，HPSEC）检测灭活禽流感病毒原液存在杂质干扰的问题，首先以H5N8型抗原为对象，分别考察了聚乙二醇（polyethylene glycol，PEG）沉淀和离子交换色谱法（ion exchange chromatography，IEC）进行预处理。在优化条件下，经DEAE FF阴离子交换层析纯化预处理，杂蛋白去除率为86.87%，病毒血凝回收率为100%。HPSEC分析预处理后的样品，8.5–10.0 min处色谱峰样品电泳检测显示主要为H5N8病毒蛋白，动态光散射分析平均粒径为127.7 nm，推测为完整病毒特征峰；在IEC预处理后的样品中加入抗体进行HPSEC检测，8.5-10.0 min处特征峰消失，显示IEC预处理有效去除了杂质干扰。通过将HPSEC与多角度激光散射技术（multi-angle laser scattering technique，MALLS）联用，可以准确获得样品中完整病毒颗粒的数量，且病毒颗粒数与色谱峰面积具有良好线性关系（R²=0.997）。建立的IEC预处理-HPSEC-MALLS检测方法应用于其他亚型（H7N9）、批次和浓度的病毒原液中完整病毒颗粒数的准确检测，均具有良好适用性，且重复性好，相对标准偏差（relative standard deviation，RSD）<5%，n=3。     

Propagation of recombinant vaccinia virus in HeLa cells: adsorption kinetics and replication in batch cultures.

The influence of various culture parameters on infection and replication of recombinant vaccinia virus in HeLa cells was examined during various phases of viral replication. A modified form of the model of Valentine and Allison (Biochim. Biophys. Acta 1960, 40, 393-399) model was used to predict successfully the viral adsorption rates in cell suspensions. An experimentally determined aggregation factor, epsilon, was included in the model to account for deviations of the observed adsorption rates from those predicted by the earlier model. It was also shown that the ionic strength, ionic species, and serum proteins present in the medium significantly altered the adsorption kinetics of the virus. The lysosomotropic base chloroquine was found to enhance viral infection more than 2-fold during the penetration step of viral infection. It was also demonstrated that cells infected during the exponential growth phase gave higher viral yields than those infected during the lag or stationary growth phases and the initial viral MOI did not significantly alter viral yields. Finally, it was demonstrated that viral infection of HeLa cells grown in 4-L bioreactor batch cultures resulted in increased death and glucose uptake rates and significantly lower growth rates.     

Impaired pulmonary oxygen uptake kinetics and reduced peak aerobic power during small muscle mass exercise in heart transplant recipients.

We examined peak and reserve cardiovascular function and skeletal muscle oxygenation during unilateral knee extension (ULKE) exercise in five heart transplant recipients (HTR, mean +/- SE; age: 53 +/- 3 years; years posttransplant: 6 +/- 4) and five age- and body mass-matched healthy controls (CON). Pulmonary oxygen uptake (Vo(2)(p)), heart rate (HR), stroke volume (SV), cardiac output (Q), and skeletal muscle deoxygenation (HHb) kinetics were assessed during moderate-intensity ULKE exercise. Peak exercise and reserve Vo(2)(p), Q, and systemic arterial-venous oxygen difference (a-vO(2diff)) were 23-52% lower (P < 0.05) in HTR. The reduced Q and a-vO(2diff) reserves were associated with lower HR and HHb reserves, respectively. The phase II Vo(2)(p) time delay was greater (HTR: 38 +/- 2 vs. CON: 25 +/- 1 s, P < 0.05), while time constants for phase II Vo(2)(p) (HTR: 54 +/- 8 vs. CON: 31 +/- 3 s), Q (HTR: 66 +/- 8 vs. CON: 28 +/- 4 s), and HHb (HTR: 27 +/- 5 vs. CON: 13 +/- 3 s) were significantly slower in HTR. The HR half-time was slower in HTR (113 +/- 21 s) vs. CON (21 +/- 2 s, P < 0.05); however, no significant difference was found between groups for SV kinetics (HTR: 39 +/- 8 s vs. CON 31 +/- 6 s). The lower peak Vo(2)(p) and prolonged Vo(2)(p) kinetics in HTR were secondary to impairments in both cardiovascular and skeletal muscle function that result in reduced oxygen delivery and utilization by the active muscles.     

Removal of thallium from aqueous solutions by modified Aspergillus niger biomass

The present study involves an investigation of various treated fungal biomasses of Aspergillus niger for the removal of thallium from aqueous solutions. Batch pH and kinetic studies were carried out to examine the effects of pH and contact time on the adsorption process. Among various pH values studied, the optimum pH was found to be between 4 and 5. The equilibrium time for Tl adsorption was found to be 6h and the rate of Tl adsorption was rapid in the initial hours. Both Lagergren's pseudo first-order model and Ho's pseudo second-order model well described the reaction kinetics. Batch adsorption experiments conducted at room temperature (22+/-1 degrees C) showed that the adsorption pattern followed the Freundlich isotherm model. Column studies using iron oxide-coated immobilized fungal biomass showed lower adsorption capacities compared to batch studies.     

Insights into adenoviral vector production kinetics in acoustic filter-based perfusion cultures

One of the major limitations in the production of adenoviral vectors is the reduction in cell-specific productivity observed for increasing cell density at infection in batch cultures. This observation strongly suggests some nutrient depletion and/or metabolite inhibition in the media. These limitations have been partially overcome through other feeding strategies, such as fed-batch and sequential batch operations. To improve these results, we evaluated perfusion as a strategy to increase the volumetric productivity of HEK-293 cell cultures, by allowing productive infection at higher cell densities. An acoustic cell separator was employed in consideration of the increased shear sensitivity of the cells during the infection phase. The effects of perfusion rate and cell density at infection on the production of a recombinant adenovirus expressing the GFP were investigated. The perfusion mode allowed successful infection at cell densities in the range of 2.4-3 x 10(6) cell/mL, while maintaining a similar cell specific productivity (17,900 +/- 2400 VP/cell) to that of a batch infected at a low cell density (5 x 10(5) cell/mL). The highest virus concentrations (4.1 +/- 0.6 x 10(10) VP/mL) were attained for a feed rate of 2 vol/d and constituted a fivefold increase compared to a batch with medium replacement. Rapid assessment of the infection status was achieved through the use of on-line monitoring of respiration, fluorescence, and biovolume. Analysis of the kinetics of nutrient consumption and metabolite production revealed that a reduction in specific productivity is correlated with reduced metabolic activity.     

Adsorption of plantaricin Q7 on montmorillonite and application in feedback regulation of plantaricin Q7 synthesis by Lactobacillus plantarum Q7

Kieselguhr, bentonite, and montmorillonite were investigated as potential carriers of plantaricin Q7. Highest level of adsorption of plantaricin Q7 was obtained with montmorillonite. Meanwhile, visible inhibition zones were observed against Listeria monocytogenes for montmorillonite adsorbed with plantaricin Q7. Adsorption kinetics showed that the adsorption behaviour followed the pseudo‐first‐order and Weber's intra‐particle diffusion models, suggesting two steps had taken place during the adsorption process. X‐ray diffraction assays revealed that plantaricin Q7 was intercalated into the interlayer space of montmorillonites. Electrostatic, hydrogen bonding and hydrophobic interactions proved to play important roles in the mechanisms of interaction between montmorillonite and plantaricin Q7, as shown by infrared spectroscopy analysis. In addition, plantaricin Q7 production was inhibited by feedback regulation with its high concentrations. In order to remove product feedback inhibition in plantaricin Q7 production, a strategy was implemented for its adsorption onto montmorillonite during fermentation. The final plantaricin Q7 output reached 3713.40 IU/mL during fermentation using montmorillonite to adsorb plantaricin Q7, 41.61% higher than that of non‐ montmorillonite. These results indicate that montmorillonites are suitable carriers for plantaricin Q7 adsorption, and the adsorption of plantaricin Q7 onto montmorillonite during fermentation could be a good method to increase final plantaricin Q7 production.     

Expanded and packed bed albumin adsorption on fluoride modified zirconia

The expanded bed characteristics of 75-103microm fluoride-modified zirconia (FmZr) particles synthesized by a fed batch oil emulsion process were investigated. These particles are distinguished from commercially available expanded-bed adsorbents by virtue of their high density (2.8 g/cc) and the mixed mode protein retention mechanism which allows for the retention of both cationic and anionic proteins. The linear velocity versus bed porosity data agree with the Richardson-Zaki relationship with the terminal velocity in infinite medium of 2858.4 cm/h and a bed expansion index of 5.1. Residence time distribution (RTD) studies and bovine serum albumin (BSA) adsorption studies were performed as a function of the height of the settled bed to the column diameter (H:D) ratio and degree of bed expansion with superficial velocities of 440 to 870 cm/h. The settled bed, a 2x expanded bed, and a 3x expanded bed were studied for the H:D ratios of 1:1, 2:1, and 3:1. The dynamic binding capacity (DBC) at 5% breakthrough was low (2-8 mg BSA/mL settled bed) and was independent of the H:D ratio or the degree of bed expansion. The saturation DBC was 32.3 +/- 7.0 mg BSA/mL settled bed. The adsorption-desorption kinetics and intraparticle diffusion for protein adsorption on FmZr (38-75 micrometer) were investigated by studying the packed bed RTD and BSA adsorption as a function of temperature and flow rate. The data show that the adsorption-desorption kinetics along with intraparticle diffusion significantly influence protein adsorption on FmZr. Low residence times ( approximately 0.8 min) of BSA result in a DBC at 5% breakthrough which is 3.5-fold lower compared to that at 6-fold higher protein residence time. At low linear velocity (45 cm/h) the breakthrough curve is nearly symmetrical and becomes asymmetrical and more dispersed at higher linear velocity (270 cm/h) due to the influence of slow adsorption-desorption kinetics and intraparticle diffusion.Copyright 1998 John Wiley & Sons, Inc. Bioeng 60: 333-340, 1998.     

Purification of a functional gene therapy vector derived from Moloney murine leukaemia virus using membrane filtration and ceramic hydroxyapatite chromatography

The ability of membrane ultra- and diafiltration and two chromatography media, Matrex Cellufine Sulfate (Millipore) and Macro-Prep ceramic hydroxyapatite (Bio-Rad), to adsorb, elute, and purify gene therapy vectors based on Moloney murine leukaemia virus (MoMuLV) carrying the 4070A amphotropic envelope protein was studied. Membrane ultra- and diafiltration provided virus concentration up to 160-fold with an average recovery of infectious viruses of 77 +/- 14%. In batch experiments, Macro-Prep ceramic hydroxyapatite (type 2, particle size 40 microm) proved superior to Matrex Cellufine Sulfate for MoMuLV vector particle adsorption. Furthermore, functional vector particles could be eluted using phosphate buffer pH 6.8 (highest titres from >or=300 mM phosphate) from the Macro-Prep adsorbent, with higher specific titres (cfu/mg protein) than the starting material. Similar results were obtained when this ceramic hydroxyapatite was packed into a column and used in a liquid chromatography system. Recovery of transduction-competent virus was between 18 and 31% for column experiments and 32 and 46% for batch experiments.     

Effect of seminal phospholipid-binding proteins and follicular fluid on bovine sperm capacitation.

Bovine seminal plasma (BSP) contains a family of novel phospholipid-binding proteins (BSP-A1/-A2, BSP-A3, and BSP-30-kDa; collectively called BSP proteins) that potentiate sperm capacitation induced by heparin or by serum high-density lipoprotein (HDL). BSP proteins stimulate lipid efflux from sperm that may occur during the early events of capacitation. Here, we investigated the role of BSP proteins, bovine follicular fluid (FF), and bovine follicular fluid HDL (FF-HDL) in sperm capacitation. FF and FF-HDL alone stimulated epididymal sperm capacitation (19.5% +/- 0.8% and 18.2% +/- 2.8%, respectively, control, 9.0% +/- 1.9%) that was increased by preincubation with BSP-A1/-A2 proteins (30.2% +/- 0.4% and 30.9% +/- 1.5%, respectively). In contrast, lipoprotein-depleted follicular fluid (LD-FF) alone was ineffective, and a preincubation with BSP-A1/-A2 proteins was necessary before sperm capacitation was stimulated (up to 22.8% +/- 1.4%). The interaction of BSP proteins with FF components was analyzed using ultracentrifugation, Lipo-Gel electrophoresis, SDS-PAGE, and gel filtration. We established that the BSP proteins interact with factors present in FF including FF-HDL. Additionally, we obtained evidence that BSP proteins, found associated with FF-HDL, were released from the sperm membrane during capacitation. These results confirm that the BSP proteins and the FF-HDL play a role in sperm capacitation.     

A highly efficient integrated chromatographic procedure for the purification of recombinant hepatitis B surface antigen from Hansenula polymorpha

The high expression level of recombinant hepatitis B surface antigen obtained from Hansenula polymorpha yeast cell (Hans-HBsAg) made it possible to produce HBsAg vaccine in a large scale and by cost-effective process. However, the present available purification process was somewhat tedious, time-consuming and difficult to scale up. To improve the purification efficiency and simplify the purification process, an integrated chromatographic process was developed and optimized. The downstream process included ion-exchange chromatography (IEC), hydrophobic interaction chromatography (HIC) and gel filtration chromatography (GFC). A series of chromatographic adsorbents were evaluated for their performances on the purification of Hans-HBsAg, and then the suitable adsorbents for IEC and HIC were screened out, respectively. After clarification by centrifugation, the supernatant of cell disruption (SCD) was purified by standard chromatographic steps, IEC on DEAE Sepharose FF, HIC on Butyl-S-QZT and GFC on Sepharose 4FF. Furthermore, HBsAg recovery, purification factor (PF) and purity during the downstream process were evaluated with enzyme-linked immunosorption assay (ELISA), sodium dodecyl sulphate-polyacrylamide gel electrophoresis (SDS-PAGE) and high-performance size-exclusion chromatography (HPSEC). The results demonstrated that in the scale of 550ml SCD, the total HBsAg recovery and PF of the whole procedure were about 21.0+/-0.9% and 80.7+/-8.4 (n=3) respectively, with the purity of above 99%. This new downstream process was efficient, reproducible and relatively easy to be scaled up.     

Ovarian modulators of 11beta-hydroxysteroid dehydrogenase (11beta HSD) activity in follicular fluid from bovine and porcine large antral follicles and spontaneous ovarian cysts

In the ovary, cortisol is oxidized to cortisone by 11beta-hydroxysteroid dehydrogenase (11betaHSD). The present study investigated whether follicular fluid (FF) from large antral follicles and spontaneous ovarian cysts, isolated from bovine and porcine ovaries, contained modulators of 11betaHSD activity. Whereas FF from antral follicles had no significant effect over 1 h on NADP+-dependent 11betaHSD activity in rat kidney homogenates, enzyme activity was inhibited by FF from bovine and porcine ovarian cysts (80.5% +/- 2.3% and 72.8% +/- 3.4% of control, respectively). Following C18 reverse-phase chromatography, the hydrophilic fractions of FF from bovine and porcine antral follicles stimulated NADP+-dependent 11betaHSD activities (111.5% +/- 21.6% and 55.2% +/- 5.7% respectively). Hydrophobic compounds inhibited NADP+-dependent cortisol oxidation by 58.2% +/- 5.1% (bovine) and 45.7% +/- 2.0% (porcine). In both species, FF from ovarian cysts appeared to contain less of the hydrophilic stimuli to 11betaHSD activity and more of the hydrophobic inhibitors. The FF from antral follicles and ovarian cysts, and the C18 fractions thereof, had no significant effect on NAD+-dependent cortisol oxidation. The ovarian modulators of NADP+-dependent 11betaHSD activities did not coelute with cortisol, cortisone, estradiol, testosterone, progesterone, pregnenolone, and cholesterol. However, the 11betaHSD stimuli in porcine FF from both antral follicles and cysts coeluted with prostaglandin (PG) E2 and PGF2alpha. We conclude that large antral follicles and spontaneous ovarian cysts, in both the cow and the pig, contain ovarian modulators of the NADP+-dependent 11betaHSD activity. Moreover, FF from spontaneous ovarian cysts, because of decreased content of the 11betaHSD stimulus accompanied by increased content of the 11betaHSD inhibitors, exerts a net inhibitory effect on 11betaHSD activity.     

Muscle capillary blood flow kinetics estimated from pulmonary O2 uptake and near-infrared spectroscopy.

The near-infrared spectroscopy (NIRS) signal (deoxyhemoglobin concentration; [HHb]) reflects the dynamic balance between muscle capillary blood flow (Q(cap)) and muscle O(2) uptake (Vo(2)(m)) in the microcirculation. The purposes of the present study were to estimate the time course of Q(cap) from the kinetics of the primary component of pulmonary O(2) uptake (Vo(2)(p)) and [HHb] throughout exercise, and compare the Q(cap) kinetics with the Vo(2)(p) kinetics. Nine subjects performed moderate- (M; below lactate threshold) and heavy-intensity (H, above lactate threshold) constant-work-rate tests. Vo(2)(p) (l/min) was measured breath by breath, and [HHb] (muM) was measured by NIRS during the tests. The time course of Q(cap) was estimated from the rearrangement of the Fick equation [Q(cap) = Vo(2)(m)/(a-v)O(2), where (a-v)O(2) is arteriovenous O(2) difference] using Vo(2)(p) (primary component) and [HHb] as proxies of Vo(2)(m) and (a-v)O(2), respectively. The kinetics of [HHb] [time constant (tau) + time delay [HHb]; M = 17.8 +/- 2.3 s and H = 13.7 +/- 1.4 s] were significantly (P < 0.001) faster than the kinetics of Vo(2) [tau of primary component (tau(P)); M = 25.5 +/- 8.8 s and H = 25.6 +/- 7.2 s] and Q(cap) [mean response time (MRT); M = 25.4 +/- 9.1 s and H = 25.7 +/- 7.7 s]. However, there was no significant difference between MRT of Q(cap) and tau(P)-Vo(2) for both intensities (P = 0.99), and these parameters were significantly correlated (M and H; r = 0.99; P < 0.001). In conclusion, we have proposed a new method to noninvasively approximate Q(cap) kinetics in humans during exercise. The resulting overall Q(cap) kinetics appeared to be tightly coupled to the temporal profile of Vo(2)(m).