目的观察β-catenin/Slug信号特异性抑制剂FH535与EMT的关系,探讨LPCAT1在调节子宫颈癌细胞侵袭、转移和生长中的作用。方法采用sh-NC和sh-LPCAT1转染Hela细胞,利用载体(Vector)组和LPCAT1过表达质粒转染SiHa细胞,将SiHa细胞分为对照组(...目的观察β-catenin/Slug信号特异性抑制剂FH535与EMT的关系,探讨LPCAT1在调节子宫颈癌细胞侵袭、转移和生长中的作用。方法采用sh-NC和sh-LPCAT1转染Hela细胞,利用载体(Vector)组和LPCAT1过表达质粒转染SiHa细胞,将SiHa细胞分为对照组(Con)、LPCAT1组、LPCAT1+FH535组和FH535组。运用CCK-8法和集落形成试验检测子宫颈癌细胞的增殖。通过伤口愈合试验和Transwell实验检测子宫颈癌细胞的转移、侵袭能力。应用Western blot分析细胞中LPCAT1、β-catenin/Slug信号通路和EMT相关蛋白的表达。结果与Vector组相比,LPCAT1组SiHa细胞的活力、集落数、迁移和侵袭细胞数均显著增加(P<0.05);与sh-NC组相比,sh-LPCAT1组Hela细胞的活力、集落数、迁移和侵袭细胞数均显著降低(P<0.05)。与LPCAT1组相比,LPCAT1+FH535组SiHa细胞中Wnt4(1.18±0.05 vs 0.80±0.06)、β-catenin(1.05±0.08 vs 0.77±0.05)、Slug(1.13±0.06 vs 0.28±0.02)、Cyclin D1(0.99±0.06 vs 0.44±0.02)、N-cadherin(0.91±0.07 vs 0.46±0.03)和vimentin(0.95±0.06 vs 0.49±0.03)表达降低(P<0.05),E-cadherin(0.44±0.03 vs 0.58±0.03)表达增加(P<0.05)。此外,与LPCAT1组相比,LPCAT1+FH535组SiHa细胞的集落数(224±15 vs 146±11)、迁移数(85±3 vs 51±4)和侵袭数(166±10 vs 90±5)均降低(P<0.05)。结论LPCAT1表达增加可能通过激活β-catenin/Slug信号通路促进子宫颈癌的转移和进展,LPCAT1的靶向治疗有望提高子宫颈癌患者的预后。展开更多
Accurate prediction of the frictional pressure drop is important for the design and operation of subsea oil and gas transporting system considering the length of the pipeline. The applicability of the correlations to ...Accurate prediction of the frictional pressure drop is important for the design and operation of subsea oil and gas transporting system considering the length of the pipeline. The applicability of the correlations to pipeline-riser flow needs evaluation since the flow condition in pipeline-riser is quite different from the original data where they were derived from. In the present study, a comprehensive evaluation of 24prevailing correlation in predicting frictional pressure drop is carried out based on experimentally measured data of air-water and air-oil two-phase flows in pipeline-riser. Experiments are performed in a system having different configuration of pipeline-riser with the inclination of the downcomer varied from-2°to-5°to investigated the effect of the elbow on the frictional pressure drop in the riser. The inlet gas velocity ranges from 0.03 to 6.2 m/s, and liquid velocity varies from 0.02 to 1.3 m/s. A total of885 experimental data points including 782 on air-water flows and 103 on air-oil flows are obtained and used to access the prediction ability of the correlations. Comparison of the predicted results with the measured data indicate that a majority of the investigated correlations under-predict the pressure drop on severe slugging. The result of this study highlights the requirement of new method considering the effect of pipe layout on the frictional pressure drop.展开更多
In 2023, the world economy was generally sluggish, and recovery remained weak. Under the pretext of “derisking,” the United States(US)-led West has generalized economic security and engaged in punitive, exclusive, a...In 2023, the world economy was generally sluggish, and recovery remained weak. Under the pretext of “derisking,” the United States(US)-led West has generalized economic security and engaged in punitive, exclusive, and collectivized economic protectionism. Developing countries are struggling.展开更多
This article studies rising velocity of Taylor bubbles and liquid slugs in liquid nitrogen at different axial positions in upward inclined tubes by means of a high speed motion analyzer. The bottom-closed tubes in the...This article studies rising velocity of Taylor bubbles and liquid slugs in liquid nitrogen at different axial positions in upward inclined tubes by means of a high speed motion analyzer. The bottom-closed tubes in the experiments are 1.0 m long with an inner diameter of 0.014 m or 0.018 m. The tube inclines upward from 0~ to 50~ with respect to the normal. Statistical method is used to analyze the data of the Taylor bubble and the liquid slug velocity. Reflecting the effects of the inclination angle on the rising velocity of Taylor bubbles and liquid slugs, the experimental results indicate the similar trend the Taylor bubble velocity and the liquid slug velocity have: it increases first, and then decreases with the increase of the inclination angle. Moreover, with the increase of the inclination angle, the liquid slug velocity becomes greater than Taylor bubble velocity.展开更多
The hydrodynamic study of the liquid film around Taylor bubbles in slug flow has great significance for understanding parallel flow and interaction between Taylor bubbles.The prediction models for liquid film thicknes...The hydrodynamic study of the liquid film around Taylor bubbles in slug flow has great significance for understanding parallel flow and interaction between Taylor bubbles.The prediction models for liquid film thickness mainly focus on stagnant flow,and some of them remain inaccurate performance.However,in the industrial process,the slug flow essentially is co-current flow.Therefore,in this paper,the liquid film thickness is studied by theoretical analysis and experimental methods under two conditions of stagnant and co-current flow.Firstly,under the condition of stagnant flow,the present work is based on Batchelor's theory,and modifies Batchelor's liquid film thickness model,which effectively improves its prediction accuracy.Under the condition of co-current flow,the prediction model of average liquid film thickness in slug flow is established by force and motion analysis.Taylor bubble length is introduced into the model as an important parameter.Dynamic experiments were carried out in the pipe with an inner diameter of 20 mm.The liquid film thickness,Taylor bubble velocity and length were measured by distributed ultrasonic sensor and intrusive cross-correlation conductivity sensor.Comparing the predicted value of the model with the measured results,the relative error is controlled within 10%.展开更多
Large vertical pipes are key structures connecting subsea wells to offshore platforms.However,existing studies mainly focus on small vertical pipes.In a vertical acrylic pipe with 80 mm inner diameter and 11 m height,...Large vertical pipes are key structures connecting subsea wells to offshore platforms.However,existing studies mainly focus on small vertical pipes.In a vertical acrylic pipe with 80 mm inner diameter and 11 m height,a high-speed camera was used to visually research the influences of pipe diameters,liquid properties and inlet effect on air-water co-flow characteristic.Different flow regime maps of vertical pipes(diameters are in the range of 50e189 mm)were compared and the critical gas velocity of the transition boundary from bubble to slug flow tended to increase with the increase of diameters at D≥80 mm.Drift-flux models were established in different flow regimes and liquid properties have a significant effect on drift coefficients of bubble flow and slug flow(void fraction a≤0.4).The influence of inlet turbulent effect on the gas-liquid interface distribution gradually weakened and disappeared from the pipe base to 85D,where the flow was fully developed.Slug frequency has a trend of increase first and then decrease with the gas Weber numbers increasing at low liquid superficial velocities(J_(L)≤0.31 m/s).And on the basis of this law,a new slug frequency correlation was proposed.It was found that there was an exponential relationship between the ratio of lengths of Taylor bubble to slug and the void fraction.展开更多
文摘目的观察β-catenin/Slug信号特异性抑制剂FH535与EMT的关系,探讨LPCAT1在调节子宫颈癌细胞侵袭、转移和生长中的作用。方法采用sh-NC和sh-LPCAT1转染Hela细胞,利用载体(Vector)组和LPCAT1过表达质粒转染SiHa细胞,将SiHa细胞分为对照组(Con)、LPCAT1组、LPCAT1+FH535组和FH535组。运用CCK-8法和集落形成试验检测子宫颈癌细胞的增殖。通过伤口愈合试验和Transwell实验检测子宫颈癌细胞的转移、侵袭能力。应用Western blot分析细胞中LPCAT1、β-catenin/Slug信号通路和EMT相关蛋白的表达。结果与Vector组相比,LPCAT1组SiHa细胞的活力、集落数、迁移和侵袭细胞数均显著增加(P<0.05);与sh-NC组相比,sh-LPCAT1组Hela细胞的活力、集落数、迁移和侵袭细胞数均显著降低(P<0.05)。与LPCAT1组相比,LPCAT1+FH535组SiHa细胞中Wnt4(1.18±0.05 vs 0.80±0.06)、β-catenin(1.05±0.08 vs 0.77±0.05)、Slug(1.13±0.06 vs 0.28±0.02)、Cyclin D1(0.99±0.06 vs 0.44±0.02)、N-cadherin(0.91±0.07 vs 0.46±0.03)和vimentin(0.95±0.06 vs 0.49±0.03)表达降低(P<0.05),E-cadherin(0.44±0.03 vs 0.58±0.03)表达增加(P<0.05)。此外,与LPCAT1组相比,LPCAT1+FH535组SiHa细胞的集落数(224±15 vs 146±11)、迁移数(85±3 vs 51±4)和侵袭数(166±10 vs 90±5)均降低(P<0.05)。结论LPCAT1表达增加可能通过激活β-catenin/Slug信号通路促进子宫颈癌的转移和进展,LPCAT1的靶向治疗有望提高子宫颈癌患者的预后。
基金the support of the Opening Fund of State Key Laboratory of Multiphase Flow in Power Engineering(SKLMF-KF-2102)。
文摘Accurate prediction of the frictional pressure drop is important for the design and operation of subsea oil and gas transporting system considering the length of the pipeline. The applicability of the correlations to pipeline-riser flow needs evaluation since the flow condition in pipeline-riser is quite different from the original data where they were derived from. In the present study, a comprehensive evaluation of 24prevailing correlation in predicting frictional pressure drop is carried out based on experimentally measured data of air-water and air-oil two-phase flows in pipeline-riser. Experiments are performed in a system having different configuration of pipeline-riser with the inclination of the downcomer varied from-2°to-5°to investigated the effect of the elbow on the frictional pressure drop in the riser. The inlet gas velocity ranges from 0.03 to 6.2 m/s, and liquid velocity varies from 0.02 to 1.3 m/s. A total of885 experimental data points including 782 on air-water flows and 103 on air-oil flows are obtained and used to access the prediction ability of the correlations. Comparison of the predicted results with the measured data indicate that a majority of the investigated correlations under-predict the pressure drop on severe slugging. The result of this study highlights the requirement of new method considering the effect of pipe layout on the frictional pressure drop.
文摘In 2023, the world economy was generally sluggish, and recovery remained weak. Under the pretext of “derisking,” the United States(US)-led West has generalized economic security and engaged in punitive, exclusive, and collectivized economic protectionism. Developing countries are struggling.
基金National Natural Science Foundation of China (50476015)
文摘This article studies rising velocity of Taylor bubbles and liquid slugs in liquid nitrogen at different axial positions in upward inclined tubes by means of a high speed motion analyzer. The bottom-closed tubes in the experiments are 1.0 m long with an inner diameter of 0.014 m or 0.018 m. The tube inclines upward from 0~ to 50~ with respect to the normal. Statistical method is used to analyze the data of the Taylor bubble and the liquid slug velocity. Reflecting the effects of the inclination angle on the rising velocity of Taylor bubbles and liquid slugs, the experimental results indicate the similar trend the Taylor bubble velocity and the liquid slug velocity have: it increases first, and then decreases with the increase of the inclination angle. Moreover, with the increase of the inclination angle, the liquid slug velocity becomes greater than Taylor bubble velocity.
基金supported by National Natural Science Foundation of China(42074142,51527805)。
文摘The hydrodynamic study of the liquid film around Taylor bubbles in slug flow has great significance for understanding parallel flow and interaction between Taylor bubbles.The prediction models for liquid film thickness mainly focus on stagnant flow,and some of them remain inaccurate performance.However,in the industrial process,the slug flow essentially is co-current flow.Therefore,in this paper,the liquid film thickness is studied by theoretical analysis and experimental methods under two conditions of stagnant and co-current flow.Firstly,under the condition of stagnant flow,the present work is based on Batchelor's theory,and modifies Batchelor's liquid film thickness model,which effectively improves its prediction accuracy.Under the condition of co-current flow,the prediction model of average liquid film thickness in slug flow is established by force and motion analysis.Taylor bubble length is introduced into the model as an important parameter.Dynamic experiments were carried out in the pipe with an inner diameter of 20 mm.The liquid film thickness,Taylor bubble velocity and length were measured by distributed ultrasonic sensor and intrusive cross-correlation conductivity sensor.Comparing the predicted value of the model with the measured results,the relative error is controlled within 10%.
基金supported by the National Natural Science Foundation of China(No.51888103,No.52076175).
文摘Large vertical pipes are key structures connecting subsea wells to offshore platforms.However,existing studies mainly focus on small vertical pipes.In a vertical acrylic pipe with 80 mm inner diameter and 11 m height,a high-speed camera was used to visually research the influences of pipe diameters,liquid properties and inlet effect on air-water co-flow characteristic.Different flow regime maps of vertical pipes(diameters are in the range of 50e189 mm)were compared and the critical gas velocity of the transition boundary from bubble to slug flow tended to increase with the increase of diameters at D≥80 mm.Drift-flux models were established in different flow regimes and liquid properties have a significant effect on drift coefficients of bubble flow and slug flow(void fraction a≤0.4).The influence of inlet turbulent effect on the gas-liquid interface distribution gradually weakened and disappeared from the pipe base to 85D,where the flow was fully developed.Slug frequency has a trend of increase first and then decrease with the gas Weber numbers increasing at low liquid superficial velocities(J_(L)≤0.31 m/s).And on the basis of this law,a new slug frequency correlation was proposed.It was found that there was an exponential relationship between the ratio of lengths of Taylor bubble to slug and the void fraction.