Optimization of pretreatment methods for N-nitrosamine compounds in ready-to-eat aquatic products / 预防医学

Objective@#To optimize the pretreatment method of N-nitrosamine compounds in ready-to-eat aquatic products. @*Methods@#Market-sold ready-to-eat aquatic products were collected, homogenized and distilled by steam. The samples were extracted for 10 minutes using dispersive liquid-liquid microextraction (DLLME) with ethanol, trichloromethane and sodium chloride (3.0 g). After centrifugation, the organic phase in the lower layer was collected and subjected to gas chromatography-tandem mass spectrometry (GC-MS/MS). The six common N-nitrosamine compounds were determined in ready-to-eat aquatic products using multiple reaction monitoring mode (MRM) and quantified by the internal standard method. @*Results@#The optimized method exhibited a good linear relationship at concentrations of 10.0 to 500 μg/L for determination of 6 N-nitrosamine compounds (correlation coefficient of greater than 0.999), with 0.05 to 0.60 μg/kg limit of detection, 0.15 to 1.60 μg/kg limit of quantitation, mean spiked recovery rates of 71.8% to 108.9%, and relative standard deviations of 1.4% to 8.6%. N-Nitrosodimethylamine showed the highest detection rate in 20 market-sold ready-to-eat aquatic products (90%), and the detection rates of N-Nitrosopyrrolidine, N-Nitrosodiethylamine and N-dibutylnitrosamine were 15%, 10% and 10%, respectively. @*Conclusion@#Steam distillation combined with DLLME may optimize the pretreatment method of N-nitrosamine compounds in ready-to-eat aquatic products and meet the measurement requirements.

Optimization of extraction technology of volatile oil from Blumea balsamifera and analysis on its compositions / 中国药房

OBJECTIVE To opti mize the supercritical CO 2 extraction technology of volatile oil from Blumea balsamifera ，and compare the components of the volatile oil from B. balsamifera obtained by supercritical CO 2 extraction and steam distillation. METHODS The volatile oil of B. balsamifera was extracted by supercritical CO 2 extraction. Using extraction rate of volatile oil as index，extraction temperature ，extraction pressure and extraction time as factors ，based on single-factor experiment ，orthogonal experiment was used to optimize the supercritical CO 2 extraction technology. Gas chromatography-mass spectrometry was used to identify the components of volatile oil from B. balsamifera . Peak area normalization was used to calculate the relative contents of each component. Taking the volatile oil obtained by steam distillation as a reference ，the extraction rates ，components and contents of volatile oil by the two methods were compared. RESULTS The optimal supercritical CO 2 extraction technology of volatile oil from B. balsamifera included extraction pressure of 30 MPa，extraction temperature of 50 ℃ and extracting for 50 min. After 3 times of validation tests ，average extraction rate of volatile oil was 4.64％（RSD＝0.54％，n＝3）. Thirty-nine components such as tritriacontane，stigmasterol，squalene were identified in the volatile oil of B. balsamifera obtained by supercritical CO 2 extraction； and 51 components such as triacontane ，ledol，humulene epoxide Ⅰ were identified by steam distillation. The extraction rate of volatile oil from B. balsamifera obtained by 2 methods were 4.64％ and 0.99％. A total of 26 common components were obtained ， such as xanthoxylin ，L-borneol，β-caryophyllene. Except for xanthoxyline （34.829％ by supercritical CO 2 extraction，30.676％ by steam distillation method ）and phytol （2.401％ by supercritical CO 2 extraction，1.273％ by steam distillation ），the relative contents of the components of volatile oil obtained by supercritical CO 2 extraction were lower than those of steam distillation. CONCLUSIONS The optimal supercritical CO 2 extraction technology is stable and feasible ；the components and contents of volatile oil obtained by two methods varies greatly ，and main compounds are aldehydes and ketones ，alkenes，alcohols and other components.

Fatores relacionados à qualidade do vapor para esterilização de produtos para saúde / Factors related to quality of steam for sterilization of medical devices / Factores relacionados con la calidad del vapor para la esterilización de productos sanitarios

Objetivos: Identificar e discutir os fatores relacionados à qualidade do vapor e sua relação com as práticas do cotidiano do Centro de Material e Esterilização. Método: Pesquisa documental, construída com base na análise do referencial teórico normativo sobre a qualidade do vapor para esteriliza-ção de produtos para saúde. Resultados: Os fatores que estão diretamente relacionados à qualidade do vapor são: água de alimentação, contaminantes do vapor, flutuações de pressão na rede, gases não condensáveis, título e superaquecimento. Conclusão: O controle de fatores que impactam o sucesso de esterilização por vapor não é uma atribuição única da engenharia clínica, mas sim uma responsabilidade compartilhada com o gestor do centro de materiais. A segurança na esterilização pelo vapor não deve ser reduzida ao controle de tempo, à temperatura ou ao resultado de indicadores físicos, quí-micos e biológicos, mas incluir o controle da qualidade do vapor, que é o agente esterilizante.

Objectives: To identify and discuss the factors related to quality of steam and their relation to daily practices of the Central Sterile Supply Department (CSSD). Method: Documentary research based on the analysis of the normative theoretical framework about quality of steam for the ste-rilization of medical devices. Results: Factors that are directly related to quality of steam are: feedwater, steam contaminants, pipeline pressure fluctua-tions, non-condensable gases, steam dryness and superheating. Conclusion: Controlling factors that impact the success of steam sterilization is not an assignment for clinical engineering service only; it is a responsibility that should be shared with the manager of the CSSD. Safety in steam sterilization should not be reduced to monitoring of time, temperature or the result of physical, chemical and biological indicators, but include monitoring of the quality of steam, which is the sterilizing agent.

Objetivos: Identificar y discutir los factores relacionados con la calidad del vapor y su relación con las prácticas cotidianas en el Centro de Material y Esterilización. Método: Investigación documental, construida a partir del análisis del marco teórico normativo sobre la calidad del vapor para esterilización de productos sanitarios. Resultados: Los factores que están directamente relacionados con la calidad del vapor son: agua de alimentación, contaminantes del vapor, fluctuaciones de presión en la red, gases no condensables, titulación y sobrecalentamiento. Conclusión: El control de los facto-res que impactan el éxito de la esterilización por vapor no es una tarea única de la ingeniería clínica, sino una responsabilidad compartida con el gerente del centro de materiales. La seguridad en la esterilización por vapor no debe reducirse al control del tiempo, la temperatura o el resultado de indicadores físicos, químicos y biológicos, sino que debe incluir el control de la calidad del vapor, que es el agente esterilizante.

EARLY STEAM INHALATION THE FIRST CRUCIAL STEP IN COMBATING EVIL – THE COVID-19

Hot water is good for throat, but the coronavirus 2019 (COVID-19) hidden behind sinuses about 3-4 days. There was no way through which the warm water would reach behind sinuses. The virus that is hiding behind the sinuses enters the lungs within 4 to 5 days and causes respiratory problems. Inhaling vapor reaches the back of the sinuses. Steam inhalation thins mucus and clears nasal passages and reduces inflammation of the upper respiratory tract or inhibits viral replication due to the heat of the steam. The virus is paralyzed at 50 ° C. The virus becomes so weak at 60 C that it can be resisted by the human immune 0 system. The virus is completely dead at 70 °C. COVID-19 can be killed by breathing vapours through the nose and mouth, according to doctors. Symptoms of mild to moderate infection (COVID-19) usually disappear through vapor inhalation. If everyone started a week-long streaming campaign, the pandemic would end soon. The deadly COVID- 19 is likely to be eliminated if everyone inhales steam during the week. There are no negative consequences to this exercise, and it is inexpensive. This review article describes the benefits of inhalation of steam and its use as an adjunct treatment during the COVID-19 pandemic

Análise crítica das especificações técnicas em processos de licitação para aquisição de autoclaves / Critical Analysis of Technical Specifications in Bidding Processes for the Acquisition of Autoclaves / Análisis crítico de especificaciones técnicas en procesos de licitación para adquisición de autoclaves

Objetivo: Analisar as especificações técnicas em processos de licitação para aquisição de autoclaves com mais de 90 L, com base na normatização relacionada. Método: Pesquisa descritiva, documental, com abordagem quantitativa, baseada em processos de licitação disponíveis online. Resultados: Foram analisados 112 processos, dos quais 106 (94,6%) foram provenientes do Brasil e seis (5,4%) do México, Honduras, El Salvador, Panamá e Paraguai. Os documentos foram analisados de acordo com aspectos construtivos, ciclos de esterilização, itens opcionais, itens de segurança e ferramentas de gestão. Conclusão: As especificações técnicas, em sua maioria, estão desatualizadas, em alguns casos comprometendo a segurança no processo de esterilização.

Objective: To analyze technical specifications in bidding processes for the acquisition of autoclaves with more than 90 L, based on the related standards. Method: Descriptive, documentary research, with a quantitative approach, based on bidding processes available online. Results: 112 bidding processes were analyzed, of which 106 (94.6%) came from Brazil and six (5.4%) from Mexico, Honduras, El Salvador, Panama and Paraguay. The documents were assessed according to construction aspects, sterilization cycles, optional items, safety items and management tools. Conclusion: Most of the technical specifications are outdated, in some cases compromising safety in the sterilization process.

Objetivo: Analizar las especificaciones técnicas en los procesos de licitación para la adquisición de autoclaves con más de 90 L, en base a la estandarización relacionada. Método: Investigación descriptiva, documental, con enfoque cuantitativo, basada en procesos de licitación disponibles online. Resultados: Se analizaron 112 casos, de los cuales 106 (94,6%) procedían de Brasil y seis (5,4%) de México, Honduras, El Salvador, Panamá y Paraguay. Los documentos fueron analizados según aspectos constructivos, ciclos de esterilización, opcionales, elementos de seguridad y herramientas de gestión. Conclusión: La mayoría de las especificaciones técnicas están desactualizadas, en algunos casos comprometiendo la seguridad en el proceso de esterilización.

Comparison of Different Extraction Techniques of Zingiber officinale Essential Oil

Abstract This study aims to find the best conditions for the extraction of Zingiber officinale essential oil using the supercritical fluid extraction (SFE), steam distillation (SD) and hydrodistillation (HD) techniques, regarding the maximum oil yield. For the HD technique is evaluated the best ratio between plant mass and water volume and for SFE and SD the pressure condition was investigated. Principal Component Analysis (PCA) was used to evaluate the similarity between the composition of the essential oil in different pressures and extraction methods. The experimental extraction curve was plotted and three different mathematical models were used to fit the data for SD and SFE methods, obtaining the relevant mass transfer parameters. The essential oil compounds were identified by gas chromatography coupled with mass spectrometry (GC-MS), being α-zingiberene the main component with different contents (from 11.9 to 28.9%). The best condition for the SFE was 100 bar, 40 °C (0.0508 goil/gplant) with 19.34% of α-zingiberene; for the SD, 3 bar (133 °C) (0.00616 goil/gplant) with 28.9% of α-zingiberene; and HD, the volume of 750 mL (0.006988 goil/gplant) with 15.70% of α-zingiberene, all measured on a dry basis.

GC-MS analysis of extraction kinetics of volatile oil from Acori Tatarinowii Rhizoma by steam distillation / 中草药

Objective: The experiment was designed to reveal the extraction, distribution and influencing factors of volatile components in the extraction process of volatile oil from Acori Tatarinowii Rhizoma (ATR). Methods: Volatile oil of ATR was extracted by steam distillation and the extract was collected every 30 min to separate the aromatic water and volatile oil. Results: A total of 56 volatile compounds were determined, of which β-asarone, methyleugenol, cis-methylisoeugenol and γ-asarone were the main characteristic constituents. There were 41 kinds of components distributed only in water, four components only in oil and 11 kinds in both oil and water. Correlation analysis showed that the specific components in water were positively correlated with the dissolution/diffusion of the main components in water, but negatively correlated with the main components in volatile oil. The water solubility of the unique components in water was the highest. The results of radar and PCA showed that the water solubility and boiling point of the specific components in water were very high, the vapor pressure of the common components of oil and water was the highest, and the polar surface areas of the special components in oil were high. Conclusion: Affected by the physical and chemical properties of volatile component, some components specifically distributed in water increased the content of main components in the aromatic water, may resulting in volatile oil extraction process easy to "emulsification", in turn, leading to an important reason for the declining quality of volatile oil.

Comparative study on volatile oil in Rhizoma chuanxiong by steam distillation and supercritical fluid extraction / 药学实践杂志

Objective To clarify the influence of the extraction process on its active ingredients by comparing the volatile oils of Rhizoma Chuanxiong obtained under different processes. Methods The volatile oil of Rhizoma Chuanxiong was extracted by supercritical CO2 extraction (SFE) and steam distillation. The main chemical components and relative contents were identified by gas chromatography-mass spectrometry (GC-MS). Results A total of 18 common components were identified in the volatile oil samples of Chuanxiong from the two methods. In steam distillation samples, main components included phthalides (61%), monoterpenoids (25%) and sesquiterpenes (10%). In SFE samples, phthalides (97%) were major components, followed by monoterpenoids (1%),sesquiterpenes (0.4%) and other minor components. Conclusion The steam distillation retains highly volatile components in Rhizoma chuanxiong such as monoterpenoids and sesquiterpenes. For SFE approach, the phthalides were extracted more efficiently compared with other components. The effect of the extraction process on the active ingredients should be fully considered in obtained products of Rhizoma chuanxiong since the difference in constituents may result in varied effects.

Does Sterilization Affect the Push Out Bond Strength of Experimental Dentin Posts? / ¿Afecta la esterilización la fuerza de adherencia de los postes de dentina experimentales?

ABSTRACT The purpose of this preliminary study is to evaluate the push-out bond strength (PBS) of experimental dentin posts (EDPs) obtained from human and bovine teeth sterilized by autoclaving and gamma radiation. Eighty-four mandibulary premolars were obturated and divided into three post groups: the glass fiber group (Fb) human EDP group (Hm) and the bovine EDP group (Bv). Three subgroups (n=12) were obtained for each EDP groups according to the sterilization methods; no sterilization (Cnt), steam autoclaving (Aut), and gamma radiation (Rad) a total dose of 25 kGy. All posts were cemented to root canals using a dual cured resin cement (Panavia SA). After the micro slices (1mm in thickness) were obtained of each subgroup, PBS test was performed. Data were analyzed using two-way ANOVA and Tukey's multiple comparison tests (α=.05). The post type and sterilization method was significantly effective on the PBS values according to the ANOVA (P<.001). No sterilization apllied EDP groups showed significantly higher PBS values than the sterilized groups (P<.001). Bv_Cnt (9.42 ±1.31) showed significantly lower PBS values than both Fb (12.36 ±1.54) and Hm_Cnt (11.06 ±1.38) groups (P<.001). Both steam autoclaving and gamma radiation affect the PBS values and fracture modes of EDPs negatively. The bovine EDPs are not as effective as human EDPs with regard to the PBS to the root dentin.

RESUMEN El propósito de este estudio preliminar es evaluar el push-out bond strength de los postes de dentina experimentales (PDE) obtenidos de dientes humanos y bovinos esterilizados por autoclave y radiación gamma. Ochenta y cuatro premolares mandibulares fueron obturadores y se dividieron en tres grupos experimentales de postes: el grupo de fibra de vidrio (Fb) grupo PDE humano (Hm) y el grupo PDE bovino (Bv). Se obtuvieron tres subgrupos (n=12) para cada grupo de PDE según los métodos de esterilización; sin esterilización (Cnt), autoclave a vapor (Aut) y radiación gamma (Rad) con una dosis total de 25 kGy. Todos los postes se cementaron a los conductos radiculares utilizando un cemento de resina de curado doble (Panavia SA). Después de que se obtuvieron las micro rebanadas (1 mm de espesor) de cada subgrupo, se realizó una prueba de push-out bond strength. Los datos se analizaron utilizando ANOVA de dos vías y las pruebas de comparación múltiple de Tukey (α=.05). El tipo de poste y el método de esterilización fueron significativamente efectivos en los valores de push-out bond strength según el ANOVA (P <.001). Los grupos de PDE no aplicados a la esterilización mostraron valores de push-out bond strength significativamente mayores que los grupos esterilizados (p <0,001). Bv_Cnt (9.42 ±1.31) mostró valores de push-out bond strength significativamente más bajos que los grupos Fb (12.36 ±1.54) y Hm_Cnt (11.06 ±1.38) (P <.001). Tanto el autoclave al vapor como la radiación gamma afectan negativamente los valores de push-out bond strength y los modos de fractura de los PDE. Los PDE bovinos no son tan efectivos como los PDE humanos con respecto a la fuerza de adhesión a la dentina de la raíz.

Pacotes molhados: o aumento do tempo de secagem aumenta o consumo de água (recurso natural escasso)? / Paquetes mojados: el aumento del tiempo de secado aumenta el consumo de agua (recurso natural escaso)? / Wet packs: Is extending drying time increasing water (scarce natural resource) consumption?

Resumo Objetivo: Este estudo tem como objetivo comparar o consumo de água e energia em quatro configurações do ciclo (número de pulsos na fase de condicionamento, tempo de secagem e valor de ajuste da profundidade do vácuo) para esterilização a vapor. Métodos: Estudo descritivo de quatro diferentes configurações de ciclo: na configuração A, os pulsos de vácuo da fase de condicionamento foram ajustados no total de três, com a profundidade de vácuo em 90 mbar e o ponto positivo de pressão em 1500 mbar. A fase de secagem foi ajustada em 45 minutos com a profundidade de vácuo em 90 mbar. Os consumos de água e energia foram medidos durante toda a fase de condicionamento e a cada 15 minutos durante a fase de secagem. Na configuração B, a profundidade de vácuo na fase de condicionamento foi de 150 mbar e os outros parâmetros foram idênticos aos da configuração A. Nas configurações C e D, o número de pulsos de vácuo foi ajustado no total de cinco, com o ponto positivo de pressão em 1500 mbar nas duas configurações e a profundidade de vácuo de 90 mbar e 150 mbar, respectivamente. Resultados: A água consumida durante a fase de secagem teve grande impacto sobre o consumo total de água durante todo o ciclo. Conclusão: Este estudo evidenciou que o aumento do tempo de secagem para solucionar pacotes molhados aumenta o consumo de água, um recurso natural escasso, que deve ser utilizado como última opção para obter pacotes secos ao fim do ciclo.

Resumen Objetivo: Este estudio tiene el objetivo de comparar el consumo de agua y energía en cuatro configuraciones del ciclo (número de pulsos en la fase de acondicionamiento, tiempo de secado y valor de ajuste de la profundidad del vacío) para esterilización a vapor. Métodos: Estudio descriptivo de cuatro diferentes configuraciones de ciclo: en la configuración A, los pulsos de vacío de la fase de acondicionamiento se ajustaron en el total de tres, con la profundidad de vacío en 90 mbar y el punto positivo de presión en 1500 mbar. La fase de secado se ajustó en 45 minutos con la profundidad de vacío en 90 mbar. Los consumos de agua y energía fueron medidos durante toda la fase de acondicionamiento y cada 15 minutos durante la fase de secado. En la configuración B, la profundidad de vacío en la fase de acondicionamiento fue de 150 mbar y los otros parámetros fueron idénticos a los de la configuración A. En las configuraciones C y D, el número de pulsos de vacío se ajustó en el total de cinco, con el punto positivo de presión en 1500 mbar en las dos configuraciones y la profundidad de vacío de 90 mbar y 150 mbar, respectivamente. Resultados: El agua consumida durante la fase de secado tuvo un gran impacto en el consumo total de agua durante todo el ciclo. Conclusión: Este estudio evidenció que el aumento del tiempo de secado para solucionar paquetes mojados aumenta el consumo de agua, un recurso natural escaso, que debe ser utilizado como última opción para obtener paquetes secos al final del ciclo.

Abstract Objective: This study aims to compare water and power consumption in four cycle configurations (number of pulses in the conditioning phase, drying time, and vacuum depth set point) for steam sterilization. Methods: A descriptive study of four different cycle configurations: In configuration A, conditioning phase vacuum pulses were set to a total of three, with a lower vacuum set point of 90 mbar and a higher pressure set point of 1500 mbar. The drying phase was set for 45 minutes with a vacuum level of 90 mbar. Water and power consumption were measured during the entire conditioning phase, and every 15 minutes during the drying phase. In configuration B the conditioning phase vacuum set point was adjusted to 150 mbar and the other parameters were identical to configuration A. On configurations C and D, the quantity of vacuum pulses was set to five, with higher pressure adjusted to 1500 mbar in both configurations. The lower vacuum set point was adjusted to 90 mbar in configuration C and to 150 mbar in configuration D. Results: Water consumption at the drying phase had the most impact on the total water consumption for the entire cycle. Conclusion: This study shows that increasing drying time to solve wet packs will increase water consumption, a scarce natural resource, and should be the last option to achieve dry loads at the end of the cycle.

Effect of seven antioxidants on thermal stability improvement of volatile oil from curcuma longa l / 中国药学杂志

OBJECTIVE: Thermal stability of Curcuma longa L. was studied by GC-MS- analysis. The affect to Curcuma longa L.by seven antioxidants were explored. METHODS: Volatile oil of Curcuma longa L. were extracted by steam extraction and heated at different temperature. The compounds of Curcuma longa L. were analysis by GC-MS. Volatile oil were heated in different temperature and the temperature which make volatile oil most obvious changing were selected. The volatile oil was heated at 100 ℃ in different time and the time which make volatile oil most obvious changing were selected. The affect to Curcuma longa L.by seven antioxidants were explored and the antioxidant which improved thermal stability of Curcuma longa L. was selected. RESULTS: The compounds of volatile oil from Curcuma longa L. was changed most significant by heated 8 h and heated at 20 ℃.The upward trend of α-turmerone was appropriate inhibited by thymol. The downward trend of ar-curcumen was better inhibited by tocopherol. CONCLUSION: The volatile oil from Curcuma longa L. shown obvious thermal instability. The volatility compounds from volatile oil of Curcuma longa L. was changed most by heated. The thermal stability of volatile oil from Curcuma longa L. can improve by antioxidants.

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.

Applications of new methods in extraction of flavonoids from Chinese materia medica / 中草药

Flavonoids are widely found in medicinal plants, which have important medical properties. Flavonoids were proved to have many pharmacological activities, such as anti-oxidation, antitumor, antimutation, anti-inflammatory, antibacterial and anti-aging. The extraction of flavonoids is the crucial link in their clinical applications. In recent years, many emerging Chinese medicine extraction methods have also been widely used in the extraction of flavonoids. This paper reviews the current application of new methods for flavonoid extraction, in order to provide references for the extraction, development and utilization of flavonoids. These new extraction methods include supercritical fluid extraction (SFE), ultrasonic assisted extraction (UAE), microwave assisted extraction (MAE), pressurized liquid extraction (PLE), pulsed electric field (PEF) assisted extraction, enzyme assisted extraction (EAE), green solvent extraction, steam explosion assisted extraction, dynamic high pressure microfluidization (DHPM) assisted extraction, etc.

Comparison of Volatile Components in Citri Sarcodactylis Fructus from Guangdong Province Before and After Being Steamed by GC-MS / 中国实验方剂学杂志

Objective:To compare volatile components in raw products and steamed products of Citri Sarcodactylis Fructus. Method:Volatile oil in different batch of raw products and steamed products of Citri Sarcodactylis Fructus was extracted by steam distillation, and volatile components were identified by GC-MS.The determination was performed with injector temperature of 280℃, high pure helium(≥ 99.999%) as carrier gas, split ratio of 10:1, and sample size of 3 μL with temperature programming.Mass spectrum conditions included electron bombardment ion source, electron bombardment energy of 70 eV, ion source temperature of 230℃, acceleration voltage of 34.6 V, resolution of 2 500, scanning range of m/z 40-350.Peak matching, cutting and noise filtering were used in analyzing data based on GC-MS combined with orthogonal partial least square-discriminant analysis(OPLS-DA). Result:A total of 58 components were separated and identified from the different batches of raw Citri Sarcodactylis Fructus and their processed products, and 27 differential chemical components were identified by multivariate statistical analysis, among them, 15 common differential components presented different changing laws.The relative contents of α-pinene, β-pinene, p-cymene, β-linalool, L-4-terpinenol, α-terpineol, nerol, β-cyclocitral, geraniol and α-citral in raw products were higher than that of their corresponding processed products.The relative contents of β-caryophyllene, cis-α-bergamotene, γ-muurolene, γ-elemene and β-bisabolene in processed products were higher than that of their corresponding raw products. Conclusion:The content and composition of volatile components in Citri Sarcodactylis Fructus from Guangdong province have changed after being steamed.The results can provide experimental basis for expounding the processing principle and quality evaluation of Citri Sarcodactylis Fructus, and have positive significance for promoting the research and development of this Lingnan characteristic decoction pieces.

Research Progress of Granulation Technology for Taste Masking of Pharmaceutical Preparation / 中国实验方剂学杂志

In commonly used oral solid preparations, poor mouthfeel results in poor patient compliance with the drug, which in turn reduces the market competitiveness of the drug. The problem of taste masking of pharmaceutical preparations has always been one of the important problems faced by pharmaceutics. With the increasing demand for the taste of drugs, the methods of masking bad taste of drugs have gradually increased in recent years. By summarizing the relevant literature covering the bad taste of drugs, the commonly used taste masking techniques include the addition of taste masking agents, inclusion techniques, microsphere/microcapsule technology, solid dispersion technology, ion exchange technology and the like. However, in addition to the above taste masking techniques, in the manufacturing process of the solid preparation, the granulation technique also can achieve the shielding of the bad taste of the medicine, and the granulation technique is simple, and can well achieve the effect of masking the bad taste of the medicine. This paper systematically introduces the research progress of granulation technology in drug taste masking, in order to provide reference for the selection of drug taste masking technology. With the increasing demand for drug taste, drug masking technology has been paid more and more attention by the majority of preparation workers, however, there are still some problems, such as imperfect taste evaluation system and low specificity of methods. This series of problems need to be further studied and solved by relevant pharmaceutical researchers.

Optimization of the Extraction Technology of Volatile Oil from Schizonepeta tenuifolia and Forsythia suspensa / 中国药房

OBJECTIVE： To establish the method for content determination of volatile oil of Schizonepeta tenuifolia and Forsythia suspensa， and to optimize the extraction technology of the volatile oil. METHODS： The contents of β-pinene and pulegone were determined by GC method. The determination was performed on Hp-5 capillary column. The detector was hydrogen flame ion detector with programmed temperature. The sample size was 0.5 μL， the split ratio was 70 ∶ 1， the carrier gas was nitrogen， the inlet temperature was 250 ℃， the detector temperature was 280 ℃， the air flow rate was 390 mL/min， the hydrogen flow rate was 36 mL/min， the tail flow rate was 15 mL/min， and the nitrogen flow rate was 1 mL/min. Based on single factor test， orthogonal test combined with information entropy method were used to optimize the extraction technology of S. tenuifolia and F. suspensa using soaking time， extraction time， material-liquid ratio and forsythia grain size as factors， with the extraction amount of volatile oil， the content of β-pinene and pulegone and their comprehensive score as indexes.  RESULTS： The linear range of β-pinene and pulegone 1.575-7.875（r＝0.999 9） and 1.892-9.46 μg（r＝0.999 7）， respectively. The limits of quantitation were 0.10 and 0.25 μg； the limits of detection were 0.03 and 0.08 μg； RSDs of precision， stability and reproducibility tests were less than 2％ （n＝6）； the recoveries were 97.77％-100.01％ （RSD＝0.93％，n＝9） and 96.47％-99.00％（RSD＝0.89％， n＝9）. The optimal extraction technology was soaking 2 h， extracting for 6 h， 10-fold water （mL/g）， half a clove of granularity. Under this condition， the extraction amount of volatile oil， the contents of β-pinene and pulegone were 3.6 mL， 1 450.4 mg， 127.6 mg， respectively. RSD were 1.62％， 0.20％， 1.42％. CONCLUSIONS： Established method is simple， accurate and reproducible， and the optimal extraction technology is stable and feasible.

Dry sauna therapy is beneficial for patients with low back pain

BACKGROUND: Dry sauna has been very popular as an alternative therapy for promoting health among people who want to improve their health condition without relying on pharmaceuticals. The aim of this study was to investigate whether dry sauna therapy improved quality of life and reduced pain in participants with low back pain.METHODS: Study participants comprised a total of 37 consecutive patients who were over 20 years of age with low back pain. Dry sauna therapy was performed twice per day for 5 consecutive days over the course of 1 week, thus comprising a total of 10 sessions each of 15 min of exposure to a 90℃ dry sauna.RESULTS: The verbal numerical rating scale (VNRS) and Oswestry disability index (ODI) scores were significantly reduced after dry sauna therapy (P < 0.001 for both). VNRS pain scores had a median (range) of 5 (2–8) before dry sauna therapy and 3 (0–8) after dry sauna therapy. ODI scores had a median (range) of 12 (2–24) before dry sauna therapy and 8 (1–17) after dry sauna therapy. The proportion of participants who reported successful treatment (excellent + good) was 70%. No adverse effects were observed related to dry sauna therapy.CONCLUSIONS: Our results suggest that dry sauna therapy may be useful to improve quality of life and reduce pain in patients with low back pain. Therefore, pain physicians can recommend dry sauna therapy as an alternative and complimentary therapy for patients with low back pain.

Protocolo de avaliação de mudança para o processo de esterilização a vapor / Change assessment protocol for steam sterilization process / Protocolo de evaluación para el proceso de esterilización a vapor

Objetivo: Relatar a experiência da criação de um protocolo de avaliação de mudança do processo de esterilização a vapor. Método: Relato de experiência, com base no fundamento teórico e na validação de novos equipamentos do Centro de Material e Esterilização. A validação ocorreu entre maio e julho de 2016, e testou a adequação ao processo e ao material, utilizando a NBR ISO 17665-1. O protocolo contempla os principais pontos para influenciar a decisão de manter ou reavaliar o equipamento. A validação do protocolo ocorreu por cinco enfermeiros atuantes no Centro de Material e Esterilização. Resultados: O protocolo foi composto por seis ações, que exigem requalificação do equipamento, e três ações que não impactaram em nenhum ponto crítico do processo. O ponto mais crítico observado ocorreu com materiais úmidos. O protocolo foi validado pelos enfermeiros do Centro de Material e Esterilização e apresentado na forma de fluxograma. Conclusão: O protocolo favorece que enfermeiros atuem de forma crítica na manutenção corretiva e preventiva do equipamento de esterilização a vapor

Objective: To report on the experience of creating a protocol, which evaluates changes in the steam sterilization process. Method: Experience report, based on the theoretical basis and validation of new equipment at the Central Sterile Supply Department. The validation occurred between May and July of 2016, and tested the suitability of the process and the material, using ISO 17665-1. The protocol includes main points that influence the decision of whether to maintain or re-evaluate the equipment. The protocol validation was carried out by five nurses from the Central Sterile Supply Deparment. Results: The protocol was composed of six actions, which required verification of the equipment, and three actions that did not impact any critical points in the process. The most critical point observed was with wet materials. The protocol was validated by the nurses from the Central Sterile Supply Department, and presented as a flowchart. Conclusion: The protocol promotes the idea of nurses acting critically in corrective and preventive maintenance of steam sterilization equipment.

Objetivo: Informar la experiencia de la creación de un protocolo de evaluación del proceso de esterilización a vapor. Método: Relato de experiencia, basado en el fundamento teórico y en la validación de nuevos equipos del Centro de Material y Esterilización. La validación ocurrió entre mayo y julio de 2016, y probó la adecuación al proceso y al material, utilizando la NBR ISO 17665-1. El protocolo contempla los principales puntos para influir en la decisión de mantener o reevaluar el equipo. La validación del protocolo fue realizado por cinco enfermeros actuantes en el Departamento Central de Abastecimiento de Esterilización. Resultados: El protocolo fue compuesto por seis acciones, que exigen recalificación del equipo, y tres acciones que no impactan en ningún punto crítico del proceso. El punto más crítico observado ocurrió con materiales húmedos. El protocolo fue validado por los enfermeros del Departamento Central de Abastecimiento de Esterilización y presentado en forma de diagrama de flujo. Conclusión: El protocolo favorece que los enfermeros actúen de forma crítica en el mantenimiento correctivo y preventivo del equipo de esterilización a vapor.

Extraction kinetics of volatile components from Foeniculum vulgare by steam distillation / 中草药

Objective To reveal the dissolution rule of volatile oil in the extraction processfrom Foeniculum vulgare by GC-MS analysis. Methods The volatile oil of F. vulgare was extracted by steam distillation; The volatile oil/perfume system was collected at fixed time interval (30 min); The volatile oil part and perfume part were separated. Using N-docosane and methyl myrisate as double internal standard, GC-MS was selected for analysis and quantification. The main components were extracted by thermography, and the distribution regularity of components was definited. The principal components with the impact on the composition distribution were investigated according to the physical and chemical properties of the molecular weight, melting point, boiling point, and density of the compounds. Results The GC-MS analysis results concluded 123 volatile components. The main components were estragole, anethole, and (R)-(+)-limonene. There were 60 and 27 endemic components in aromatic aqueous solution and volatile oil, respectively, in which 27were common composition. The content of anethole in water was positively related to the endemic components in aromatic water, and even had a positive correlation with anethole artemisia content and (R)-(+)-limonene content. The specific components in the oil were positively related to the content of the main components (R)-(+)-limonene in the volatile oil. The principal component analysis showed that the physical and chemical properties of the compounds were important factors affecting the distribution of components; PC1 (molecular weight and positive correlation of melting point), PC2 (refractive index positive correlation), and PC3 (water-soluble negative correlation) were the principal components that lead to differences in component distribution. Conclusion In the process of extracting volatile oil from F. vulgare, steam distillation is affected by the physical and chemical properties of volatile components. Some components are specifically distributed in aromatic perfume and volatile oil system. The endemic components of aromatic water increase the content of the main components in the water system, which may lead to theproduction of "emulsification" during the extraction process of volatile oil and reduce the yield and quality of volatile oil.

Comparison of Class 5 and 6 chemical indicative cards applied to pressure steam sterilization in hospitals / 医疗卫生装备

Objective To observe the effects of Class 5 and 6 chemical indicative cards used for monitoring pressure steam sterilization to standardize the procedure for selecting the monitoring substance of pressure steam sterilization. Methods Several pieces of Class 5 and 6 cards were placed at the four corners and center of the clave to undergo sterilization with the conventional parameters of 134 ℃, 240 s and 220 kPa as well as the simulation critical parameters of 134 ℃, 120 s and 220 kPa.The two kinds of cards had their qualification rates compared with two sets of parameters.SPSS 19.0 software was used for data analysis and Chi-square test was applied to comparison.Results The two kinds of cards had the qualification rates being 100% with the conventional parameters;with the simulation critical parameters,Class 5 card had the qualification rate being 100%,while Class 6 card had the rate of 66.67%,and there were significant difference between the qualification rates of the two cards(P<0.05).Conclusion Class 6 chemical indicative card has higher resistance and efficiency with the same conditions when compared with Class 5 card,which can be combined with the tube cavity challenger to execute mass monitoring with unstable parameters.