Supercritical CO2 assisted process for the production of high-purity and sterile nano-hydroxyapatite/chitosan hybrid scaffolds.

Hybrid scaffolds composed of hydroxyapatite (HAp), in particular in its nanometric form (n-HAp), and chitosan (CS) are promising materials for non-load-bearing bone graft applications. The main constraints of their production concern the successful implementation of the final purification/neutralization and sterilization steps. Often, the used purification strategies can compromise scaffold structural features, and conventional sterilization techniques can result in material's thermal degradation and/or contamination with toxic residues. In this context, this work presents a process to produce n-HAp/CS scaffolds mimicking bone composition and structure, where an innovative single step based on supercritical CO2 extraction was used for both purification and sterilization. A removal of 80% of the residual acetic acid was obtained (T = 75°C, p = 8.0 MPa, 2 extraction cycles of 2 h) giving rise to scaffolds exhibiting adequate interconnected porous structure, fast swelling and storage modulus compatible with non-load-bearing applications. Moreover, the obtained scaffolds showed cytocompatibility and osteoconductivity without further need of disinfection/sterilization procedures. Among the main advantages, the proposed process comprises only three steps (n-HAp/CS dispersion preparation; freeze-drying; and supercritical CO2 extraction), and the supercritical CO2 extraction show clear advantages over currently used procedures based on neutralization steps. © 2017 Wiley Periodicals, Inc. J Biomed Mater Res Part B: Appl Biomater, 106B: 965-975, 2018.

Effect of cosmetic matrices on the release and odour profiles of the supercritical CO2 extract of Origanum majorana L.

OBJECTIVE: In this study, the effect of different cosmetic matrices on the release profile and odour intensity of the fragrance O. majorana was investigated for the first time. METHODS: The fragrance compounds of O. majorana were extracted by supercritical fluid extraction using carbon dioxide (SFE-CO2 ) at 40°C and two operating pressures (8.5 and 10 MPa), and their chemical profiles were assessed by gas chromatography with flame ionization detector coupled with mass spectrometry (GC-FID/MS). Lastly, the fragrance compounds were incorporated into three cosmetic matrices (glycerine, dipropylene glycol and skin lotion) to assess their release and odour profiles over time using dynamic headspace (DHS)/GC-FID/MS and Odour Value concept, respectively. RESULTS: The SFE-CO2 enabled recovering extracts with the pleasant scent of the living plant, and the increment of pressure induced an increase on the extraction yield. GC-FID/MS analyses revealed that oxygen-containing monoterpenes was the principal group of components identified in both SFE-CO2 extracts. The fragrance compounds were more retained in dipropylene glycol, and the major deviations from the original odour intensity (control) were observed in the presence of dipropylene glycol and skin lotion. CONCLUSION: The hydrophilic character of the cosmetic matrices strongly influenced the release of the fragrance compounds, thus affecting the odour profile of the studied mixtures.

Índices de eficiência reprodutiva de búfalos da Amazônia Oriental do Brasil / Indices of reproductive efficiency of buffaloes of the Brazilian Eastern Amazon

Foram avaliados registros de manejo reprodutivo de búfalos das raças Jafarabadi, Murrah, Mediterrâneo, Carabao e Tipo Baio, bem como seus mestiços, no período de 1983 a 2005. Estudaram-se as características reprodutivas: idade à primeira cria (média de 1052,52±120,45 dias), intervalo de partos (média de 399,69±23,78 dias), eficiência reprodutiva (média de 91,09±1,89%), fertilidade real adaptada (média de 29,30±4,40 quilogramas de bezerro parido por ano), produtividade ao primeiro parto adaptada (média de 33,75±6,89 quilogramas) e produtividade acumulada adaptada (média de 22,86±6,55 quilogramas de bezerro parido por ano). Foram verificadas influências do ano de parto e o grau de sangue da fêmea sobre as características estudadas, o que indica que tais efeitos devem ser incluídos na avaliação genética e na seleção dos animais. Os índices produtivos utilizados mostraram-se de grande valia para a seleção, devendo ser mais estudadas suas interações relativas ao desempenho geral do rebanho.

We evaluated records of reproductive management Jaffarabadi buffalo breeds, Murrah, Mediterranean, Carabao and Baio types, and their crosses, in the period from 1983 to 2005. We studied the following reproductive characteristics: Age at first calving (mean 1052.52±120.45 days), calving interval (399.69±23.78 mean days), Reproductive Efficiency (average 91.09±1, 89%), Real Adapted Fertility (average 29.30±4.40kg calf calved each year), the First Labor Productivity Adapted (mean 33.75±6.89kg) and Accumulated Productivity Adapted (mean 22.86±6.55kg calf calved each year). Influences were observed in the year of delivery and degree of blood on the female traits, suggesting that such effects should be included in genetic evaluation and selection of animals. The production indices used were of great value for the selection, and should be well studied for their interactions with the overall performance of the herd.

Estimação de parâmetros genéticos para características produtivas em búfalos na Amazônia Oriental / Estimation of genetic parameters of dairy buffaloes productive characteristics Eastern Amazon

Dados de 1.182 registros de produção de fêmeas bubalinas da raça Murrah e seus mestiços, parindo no período de 1967 a 2005, foram utilizados para estimação de parâmetros genéticos utilizando-se o método de máxima verossimilhança restrita. O modelo animal utilizado para estimação de componentes de variância incluiu os efeitos fixos de rebanho, ano e época de parto, ordem de parto e duração da lactação e os efeitos aleatórios do animal, e ambiente permanente e temporário. As estimativas de herdabilidade foram 0,25, 0,18, 0,08 e 0,09, para produção de leite, produção de gordura, duração da lactação e produção de leite por dia de intervalo de parto, respectivamente. As estimativas de repetibilidade foram 0,33, 0,29 e 0,10 para produção de leite, produção de gordura e duração da lactação, respectivamente. As correlações genéticas entre produções de leite e gordura, produção de leite com duração da lactação, produção de leite com produção de leite por dia de intervalo de partos, produção da gordura com duração da lactação, produção de gordura com produção de leite por dia de intervalo de partos e duração da lactação com produção de leite por dia de intervalo de partos foram 0,93; 0,76; 0,99; 0,89; 0,87 e -0,27, respectivamente. Os resultados demonstram que ganhos genéticos podem ser obtidos pela seleção das produções de leite e gordura.

Data from 1,182 records of Murrah females buffaloes and their crossbreds, calving from 1967 to 2005, were used to estimate genetic parameters by maximum restricted likelihood method. An animal model used to estimate variance components, included the fixed effects of herds, year and season of calving, order of parity, and length of lactation as covariables; and random effects of animal, permanent, and temporary environment. The estimate of heritability to milk yield, fat yield, length of lactation, and milk yield per day of calving interval were 0.25, 0.18, 0.08, and 0.09 respectively. Estimate of repeatability for milk yield, fat yield, and length of lactation were 0.33, 0.29, and 0.10, respectively. The genetic correlations between milk yield and fat yield, milk yield and length of lactation, milk yield and milk yield per day of calving interval, fat yield and length of lactation, fat yield and milk yield per day of calving interval, and length of lactation and milk yield per day of calving interval were 0.93, 0.76, 0.99, 0.89, 0.87, and -0.27, respectively. These results showed that genetic gains may be obtained by selecting to milk and fat yields.

Quantification of lactobionic acid and sorbitol from enzymatic reaction of fructose and lactose by high-performance liquid chromatography.

Experimental conditions for complete separation and quantification of mixtures containing lactobionic acid, sorbitol, lactose and fructose are discussed for the first time. These mixtures appear in the enzymatic bioconversion of fructose and lactose catalyzed by glucose-fructose oxidoreductase (GFOR) and glucono-delta-lactonase (GL) enzymes of Zymomonas mobilis cells. The high-performance liquid chromatography (HPLC) separation was carried out in a strong cation ion exchange resin (hydrogen form) based on a copolymer of styrene divinylbenzene (PS-DVB). A stationary phase of beta-cyclodextrin was also evaluated. An efficient separation was obtained with PS-DVB column eluted with sulfuric acid 0.450 mM solutions (pH 3.0-3.2) at 75 degrees C. The formation of lactones was observed, which is associated with the dissolution of lactobionic acid crystals; however, by dissolving the lactobionic acid crystals on alkaline calcium hydroxyde solution in equimolar ratio a single lactobionic acid chromatographic peak without lactobionolactone is obtained.

On the kinetics and energetics of one-electron oxidation of 1,3,5-triazines.

One-electron oxidation of 1,3,5-triazines is observed with both excited uranyl ion (*UO2(2+)) and sulfate radical anion (SO4.-) in aqueous solution, but not with Tl2+, indicating that the standard reduction potentials E degree of 1,3,5-triazine radical cations are = 2.3 +/- 0.1 V vs. NHE, consistent with theoretical calculations; this suggests that if triazines inhibit electron transfer during photosynthesis, they would need to act on the reductive part of the electron transport chain.

Adsorption of basic dyes on granular activated carbon and natural zeolite.

The adsorption of basic dyes from aqueous solution onto granular activated carbon and natural zeolite has been studied using an agitated batch adsorber. The influence of agitation, initial dye concentration and adsorbent mass has been studied. The parameters of Langmuir and Freundlich adsorption isotherms have been determined using the adsorption data. Homogeneous diffusion model (solid diffusion) combined with external mass transfer resistance is proposed for the kinetic investigation. The dependence of solid diffusion coefficient on initial concentration and mass adsorbent is represented by the simple empirical equations.

Separation of ternary mixtures by pseudo-simulated moving bed chromatography.

Modeling and simulation are presented of the separation of a ternary mixture by pseudo-simulated moving bed chromatography, according to the JO process of Japan Organo Co. The process cycle is divided into two steps. In step 1, feed and eluent streams are introduced into the system, equivalent to a series of preparative chromatographic columns, and the intermediate component is produced. In step 2, similar to a simulated moving bed (SMB), there is no feed and the less adsorbed species is collected in the raffinate while the more retained species is collected in the extract; this step is described by an equivalent TMB model. A parametric study is presented in order to analyze the sensitivity of the model to variations on the duration of step 1 and step 2 and on the intraparticle mass transfer coefficient.

Enantiomers separation by simulated moving bed chromatography. Non-instantaneous equilibrium at the solid-fluid interface.

The simulated moving bed (SMB) technology, first conceived for large bulk-scale separations in the petrochemical industry, has found increasingly new applications in the pharmaceutical industry. Among these, the separation of fine chemicals has been the subject of considerable study and research. This work presents the modeling, simulation and design of the operation of a SMB plant in order to separate a binary chiral mixture. The usual assumption of instantaneous equilibrium at the solid-fluid interface is questioned and a first-order kinetics of adsorption is taken into account. The cases of linear, Langmuir and modified Langmuir equilibria are studied. The equivalent true moving bed (TMB) model was used assuming axial dispersion for the fluid flow and plug flow for the solid-phase flow. Intraparticle diffusion was described by a linear driving force (LDF) approximation. Simulation results indicate that, under certain conditions, equilibrium is not actually reached at the adsorbent surface. This leads to different unit performances, in terms of product purities and recoveries, as compared to those predicted assuming instantaneous equilibrium. Moreover, SMB units may be improperly designed by the usual methods (flow-rate ratio separation regions) if non-equilibrium effects are overlooked.

Permeable packings and perfusion chromatography in protein separation.

The use of permeable packings in perfusion chromatography for protein separation is reviewed. Mass transport mechanisms in large-pore materials include forced convection in addition to diffusive transport. The key concept in perfusion chromatography is the "augmented" diffusivity by convection which explains the improved efficiency of perfusive packings compared with conventional supports. An extended Van Deemter equation has to be applied when calculating the height equivalent to a theoretical plate (HETP) of chromatographic columns with flow-through particles. It is shown that the effect of forced convective flow in pores is to drive the separation performance between diffusion-controlled and equilibrium limits. A methodology to understand mass transfer mechanisms in permeable packings is proposed. Experimental results for protein separation by high-performance liquid chromatography in new packing media are discussed. Simulated moving bed technology is addressed.

Bioseparations with permeable particles.

Permeable large-pore particles have many applications, in particular in perfusion chromatography for bioseparations. The objective of this paper is to elucidate the mass transport mechanisms in two commercial adsorbents-POROS Q/M and Q Hyper D-and to answer the question if intraparticle convection is present as a mass transfer mechanism. The paper contains three sections. In the first part, mass transfer inside porous particles is discussed. The mass transfer mechanism which allows improved performance of perfusion chromatography is intraparticle convection. The combined effect of intraparticle convection and diffusion is an "augmented" effective diffusivity. This is the key concept to explain the peak sharpening and modified Van Deemter plots found with large-pore particles. In the second part, column efficiencies in terms of HETP as a function of bed superficial velocity are experimentally measured for a non-retained protein (bovine serum albumine, BSA) in two adsorbents: POROS Q/M (PerSeptive Biosystems) and Q Hyper D (BioSepra). In the third section breakthrough curves for both materials are measured for a test protein (BSA) from which useful capacities and productivities as a function of flow-rate are calculated. Experimental results indicate that intraparticle convection plays indeed an important role in both adsorbents.