A simulating method for dripping process of Ginkgo biloba leaf dripping pills based on computational fluid dynamics technology / 药学学报

A simulating method for dripping process of Ginkgo biloba leaf dripping pills based on computational fluid dynamics was constructed. Ginkgo biloba leaf dripping pills was explored as the experimental subject to simulate the dripping process based on FLOW-3D software. The dripping process was simulated through the derivation of the governing equations, the selection of the models, and simulation parameters. Firstly, the droplet morphologies and drop speeds under different liquid viscosity were simulated. It was found that with the increase of the liquid viscosity, the drop speed decreased and the difficulty of droplet preparation gradually increased. The simulation results were consistent with the experiment results. Secondly, the droplet morphologies at different drop speeds were investigated and verified by experiments. It was found that the simulation results had a good correlation with the experiment results. The results shown that the viscosity of the liquid was the critical material attribute, and the drop speed was the critical process parameter, according to the droplet morphology. The establishment of the simulation method can deepen the understanding of the dripping process and provide a reference for the selection of raw materials and process parameters.

Optimization of process parameters of 3D printed clozapine dispersive tablets and establishment of personalized dose model / 药学学报

This study aims to establish the design space of the key processes for drop-on-powder 3D printing based on design of experiment (DoE). By utilizing Minitab, an experimental scheme with three factors, two levels and three center points was designed to analyze the factors that significantly affected the tablet quality attributes. Furthermore, the factor interactions were analyzed using Minitab. subsequently, the computer aided drafting (CAD) software was used to adjust the model volume with fixed radius/height ratio (r/h = 1.25) and establish a linear regression equation between model volume and dose. As a result, the drug dose could be controlled in a flexible manner. The finally determined process parameters were: ink-jet level is 12, layer thickness is 150 μm, and the X-axis printing head speed of 635 mm·s-1. Regression equation between drug content (y) and model volume (x) was y = 0.062 x - 0.582 7 (R2 = 0.999 9) showing good linear relationship. This indicated that robust and feasible process parameters were obtained through DoE, and the preparation of personalized-dose tablets was realized with good reproducibility.

Study on extraction kinetics of Salviae Miltiorrhizae Radix et Rhizoma: model establishment and investigation of critical process parameters / 中国中药杂志

In this study, Fick's first law and partition equilibrium were used to represent the internal and external mass transfer processes of Salviae Miltiorrhizae Radix et Rhizoma at the macroscopic level, and a mass transfer model was established. The specific surface area was integrated into the mass transfer resistance, which effectively avoided the irregular shape of medicinal materials and expanded the application scope of the model. Meanwhile, the mass transfer model was further combined with the kinetic model of salvia-nolic acid degradation to establish the extraction kinetic models of salvianolic acid B, lithospermic acid and Danshensu. The model was applied to study the extraction process of Salviae Miltiorrhizae Radix et Rhizoma. According to the sensitivity analysis results, the relative error of the model prediction was within 5% near the maximum extraction rate(320 min), and the prediction performance of the model was good. According to the investigation results of different process parameters, stirring could significantly accelerate the mass transfer rate of salvianolic acid B, while the mass transfer resistance and degradation rate constant were not affected by solvent-to-solid ratio. The linear relationship between the reciprocal of temperature and the logarithm of mass transfer resistance was good(R~2=0.996), indicating that the temperature and mass transfer resistance conformed to Arrhenius formula. In addition, we also found that the concentration changes of lithospermic acid and Danshensu were weakly affected by mass transferwhen the extraction temperature was higher than 358 K. This study has provided the basis for the process optimization and quality control of traditional Chinese medicine extraction.

Quality control of ethanol extraction process of Corydalis Rhizoma based on quality by design (QbD) / 中草药

Objective: To improve the quality control level of ethanol extraction process of Corydalis Rhizoma (CR) by using quality by design (QbD), so as to meet the extraction requirements of Kedaling Tablets. Methods: The critical process parameters were solvent multiple, extraction time and soaking time, and the critical quality attributes were dry extract rate, content and transfer rate of dehydrocorydaline. The response surface methodology was used to establish the mathematical model between the critical process parameters and the critical quality attributes. The overlapping design space of multiple index design spaces was established to select the optimal operation space, where the process verification was carried out. Results: The operating space parameters of ethanol extraction of CR was 14-24 h of the immersion time, 3.0-4.0 times of the first time solvent multiple, 1.5-2.0 times of the second and third time solvent multiple, and 1.5-2.5 h of the extraction time. Under this operating space, the extraction yield of CR was ranged from 6%-8%, the content of dehydrocorydaline was more than 2.8%, and the transfer rate was not less than 85%. Conclusion: The concept of QbD is helpful to improve the ethanol extraction process of CR, and to obtain a reliable and suitable extraction operation space for the production of Kedaling Tablets.

The investigation of key factors influencing the extraction process of chuanxiong oil by steam distillation / 中国药学杂志

OBJECTIVE: To investigate the key process parameters that affect the extraction of essential oil from Ligusticum chuanxiong by steam distillation. METHODS: Volatile oil and emulsified aromatic water are the products of the extraction process of volatile oil. The nature of volatile oil will directly affect the formation of emulsified aromatic water. The influence of extraction temperature, the ratio of liquid to medicine, medicinal material granularity process parameters on the stability of the emulsified fragrance water and the yield of volatile oil were analyzed, furtherly the corresponding extraction process control model of volatile oil was established to reveal the key technology and parameter during the process of volatile oil extraction and separation. RESULTS: The relative viscosity, relative density, surface tension and contact angle of Ligusticum chuanxiong oil decreased gradually with the increase of temperature, while the interfacial tension increased with the increase of temperature. The liner model of aromatic water TSI and process parameters was TSI = 0. 877 + 0. 230 × extraction temperature - 0. 024 × comminution particle size + 0. 010 × liquid ratio + 0. 292 × condensation temperature + 0. 776 × collection temperature. The liner model of the physicochemical properties of TSI and volatile oil was TSI = 0. 877 - 0. 170 × density + 0. 098 × viscosity - 0. 301 × surface tension + 0. 695 × interfacial tension - 0. 060 × contact angle. The liner model of volatile oil yield and process parameters was that yield = 5. 065 + 0. 258 × extraction temperature + 0. 127 × particle size + 0. 016 × liquid ratio + 0. 264 × condensation temperature + 0. 264 × collection temperature + 0. 502 × TSI. The liner model with the physicochemical properties of volatile oil was the yield = 5. 065 - 0. 196 × density - 0. 167 × viscosity - 0. 201 × surface tension + 0. 153 × interfacial tension - 0. 065 × contact angle. CONCLUSION: TSI and yield of aromatic water of Ligusti-cum chuanxiong are directly proportional to the extraction temperature and comminution particle size of medicinal materials. The yield of volatile oil shows a significant positive correlation with the TSI value, which can reflect the yield of volatile oil and is a specific index that can evaluate the process parameters objectively.

Aplicación del Análisis de Componentes Principales en el proceso de fermentación de un anticuerpo monoclonal / Application of Principal Components Analysis in the fermentation process of a monoclonal antibody

En el Centro de Inmunología Molecular (La Habana, Cuba) se produce un anticuerpo monoclonal terapéutico que ha encontrado una efectiva aplicación en el tratamiento de pacientes aquejados de cáncer de cabeza y cuello. Dada la gran variabilidad que ha tenido la concentración de este anticuerpo en la etapa de fermentación industrial de la planta donde es producido, se hizo necesaria la aplicación de una técnica de análisis multivariante como el Análisis de Componentes Principales, con el fin de reducir la dimensionalidad de los datos y de explicar las principales fuentes de variabilidad del proceso. Para llevar a cabo el Análisis de Componentes Principales mediante el programa THE UNSCRAMBLER se partió de la determinación de los parámetros críticos de la etapa de fermentación a través de un modelo de riesgo basado en matriz de entradas y salidas empleando los datos de la campaña realizada en el año 2014. Como resultado se obtuvo que dos componentes principales logran explicar más del 99 por ciento de la varianza total, y se logró definir cuáles son los parámetros críticos que mayor aporte tienen a la variabilidad del proceso de fermentación. Dichos resultados corroboraron experiencias prácticas de especialistas de la planta y permitieron dar recomendaciones a considerar en el Plan de Verificación Continuada del Proceso, como proponer la inclusión en la estrategia de control del proceso a la temperatura, la velocidad de agitación, el oxígeno disuelto y el tiempo de duración del cultivo(AU)

In the Center of Molecular Immunology (Havana, Cuba) an effective therapeutic monoclonal antibody against head and neck cancer is produced. Given the great variability of the concentration of this antibody in the industrial fermentation stage of the plant, it became necessary to apply a multivariate analysis technique such as the Principal Component Analysis, in order to reduce data dimensionality and to explain the main sources of variability of the process. In order to carry out the Principal Component Analysis through the software THE UNSCRAMBLER, the determination of the critical parameters of the fermentation stage through a risk model based on input and output matrix using data from the campaign of the year 2014 was carried out. As a result, two main components were able to explain more than 99 percent of the total variance, and it was possible to define the critical parameters that have the greatest contribution to the variability of the fermentation process. These results corroborated the practical experiences of specialists of the plant and allowed to give recommendations to consider in the Plan of Continuous Verification of the Process as proposing the inclusion in the strategy of control of the process the variables temperature, the speed of agitation, dissolved oxygen and the culture duration(AU)

Application of quality by design in granulation process for Ginkgo leaf tablet (Ⅲ)： process control strategy based on design space / 中国中药杂志

In this paper, under the guidance of quality by design (QbD) concept, the control strategy of the high shear wet granulation process of the ginkgo leaf tablet based on the design space was established to improve the process controllability and product quality consistency. The median granule size (D50) and bulk density (Da) of granules were identified as critical quality attributes (CQAs) and potential critical process parameters (pCPPs) were determined by the failure modes and effect analysis (FMEA). The Plackeet-Burmann experimental design was used to screen pCPPs and the results demonstrated that the binder amount, the wet massing time and the wet mixing impeller speed were critical process parameters (CPPs). The design space of the high shear wet granulation process was developed within pCPPs range based on the Box-Behnken design and quadratic polynomial regression models. ANOVA analysis showed that the P-values of model were less than 0.05 and the values of lack of fit test were more than 0.1, indicating that the relationship between CQAs and CPPs could be well described by the mathematical models. D₅₀ could be controlled within 170 to 500 μm, and the bulk density could be controlled within 0.30 to 0.44 g•cm⁻³ by using any CPPs combination within the scope of design space. Besides, granules produced by process parameters within the design space region could also meet the requirement of tensile strength of the ginkgo leaf tablet..

Endophytic fungus strain 28 isolated from Houttuynia cordata possesses wide-spectrum antifungal activity

Abstract The aim of this paper is to identify and investigate an endophytic fungus (strain 28) that was isolated from Houttuynia cordata Thunb, a famous and widely-used Traditional Chinese Medicine. Based on morphological methods and a phylogenetic analysis of ITS sequences, this strain was identified as Chaetomium globosum. An antifungal activity bioassay demonstrated that the crude ethyl acetate (EtOAc) extracts of strain 28 had a wide antifungal spectrum and strong antimicrobial activity, particularly against Exserohilum turcicum (Pass.) Leonard et Suggs, Botrytis cinerea persoon and Botrytis cinerea Pers. ex Fr. Furthermore, the fermentation conditions, extraction method and the heat stability of antifungal substances from strain 28 were also studied. The results showed that optimal antifungal activity can be obtained with the following parameters: using potato dextrose broth (PDB) as the base culture medium, fermentation for 4–8 d (initial pH: 7.5), followed by extraction with EtOAc. The extract was stable at temperatures up to 80 °C. This is the first report on the isolation of endophytic C. globosum from H. cordata to identify potential alternative biocontrol agents that could provide new opportunities for practical applications involving H. cordata.

Impact of parameter fluctuations on the performance of ethanol precipitation in production of Re Du Ning Injections, based on HPLC fingerprints and principal component analysis / 中国天然药物

The present study was designed to determine the relationships between the performance of ethanol precipitation and seven process parameters in the ethanol precipitation process of Re Du Ning Injections, including concentrate density, concentrate temperature, ethanol content, flow rate and stir rate in the addition of ethanol, precipitation time, and precipitation temperature. Under the experimental and simulated production conditions, a series of precipitated resultants were prepared by changing these variables one by one, and then examined by HPLC fingerprint analyses. Different from the traditional evaluation model based on single or a few constituents, the fingerprint data of every parameter fluctuation test was processed with Principal Component Analysis (PCA) to comprehensively assess the performance of ethanol precipitation. Our results showed that concentrate density, ethanol content, and precipitation time were the most important parameters that influence the recovery of active compounds in precipitation resultants. The present study would provide some reference for pharmaceutical scientists engaged in research on pharmaceutical process optimization and help pharmaceutical enterprises adapt a scientific and reasonable cost-effective approach to ensure the batch-to-batch quality consistency of the final products.

Comparison on three methods for identification of critical process parameters / 中草药

Objective: To investigate the characteristics of multiple linear regression method, stepwise regression method, and standardized partial regression coefficient method for the identification of critical process parameters. Methods: The acid precipitation and alkaline dissolution process of Scutellariae Radix (SR) water extract was investigated as an example. Results: Similar results were obtained using three different methods. The concentration of SR water extract, pH value of acid precipitation, pH value of alkali dissolution, and refrigeration temperature were considered as critical process parameters. Conclusion: The selection of threshold values of the three methods all are subjective. Multiple linear regression method is simple, but is not as sensitive as stepwise regression method. The effects of a parameter on several process indices can be considered simultaneously and easily weighted using standardized partial regression coefficient method.

Technology Verification for Irbesartan and Hydrochlorothiazide Tablets / 中国药师

Objective: To verify the feasibility and reliability of the pilot process of irbesartan and hydrochlorothiazide tablets. Methods:Three batches of the tablets were produced according to the determined formula and process, and the key parameters in the pilot production were verified. Results:All the indices for each batch of irbesartan and hydrochlorothiazide tablets conformed to the re-quirements of the quality standard. Conclusion: The pilot process of irbesartan and hydrochlorothiazide tablets is feasible, and the technological process and parameters can ensure the product quality with promising reliability and stability.

Functionality advancement of poorly soluble biovariable anti hypertensive Drug by sophisticated SD-FBP technology as per enhanced QbD.

Lacidipine (LCDP) is a dihydropyridine derivative categorized as an Anti-hypertensive Ca+2 channel blocker belonging to BCS class IV drug with low solubility and low permeability which presents a challenge to the formulation scientists. The development of a solid dispersion by solvent evaporation is a practically viable method to enhance dissolution of LCDP from oral dosage form. Solvent evaporation by Fluidized Bed Process (FBP) was the method of choice for SD as it improves wettability with simultaneous increase in porosity of granules resulting enhanced surface area producing higher dissolution rate and bioavailability of poorly water-soluble drug. Thus, the main object of the present invention is to provide stable pharmaceutical dosage form of LCDP with desired dissolution rate i.e. at least 80% drug release within 45 minutes, without use of disintegrant(s) and/or surfactant(s) or without micronization of the active ingredient per se. One more object of this invention is to provide a sophisticated robust process for the preparation of said pharmaceutical dosage form by Quality by Design (QbD) concept focusing on thorough understanding of the product and process by which it is developed and manufactured along with a knowledge of the risks involved in manufacturing by IRMA & FMEA study of the product with process and how best to mitigate those risks by developing design space with DoE & MVDA with outlined control strategy.