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Mud pulse generators have been widely used for the real-time transmission of valuable directional and formation data from downholes with depths of thousands of meters. There have been numerous studies on the design of mud pulse generators in which the pressure waves were typically nonsinusoidal. Sinusoidal waves provide improved long-distance data transmission and signal noise suppression compared with nonsinusoidal waves. Although sinusoidal pressure wave generators have been studied in the published literature, the influence of the risks of clogging on the design of the generator for producing sinusoidal pressure waves has rarely been considered. To generate sinusoidal pressure waves and to reduce the risks of clogging, a mathematical model for the design of a sinusoidal pressure wave generator is developed in this paper. The effects of the axial and radial clearances between the rotor and stator on the design of the generator are considered in the model. An optimum design method for the generator is provided by combining the developed model and a computational fluid dynamics analysis. Finally, an experimental platform was built and experiments at frequencies 2 Hz and 10 Hz were conducted to validate the design result. The simulation and experimental results show that the optimized pressure waves closely approximate sine waves. Therefore, the developed mathematical model and optimization approach can be used to design a sinusoidal pressure wave generator. [ABSTRACT FROM AUTHOR]

A novel combustion gas and steam mixture cycle (GSMC) power generation system was simulated and studied in this paper. The system integrates the technologies of NG/O 2 combustion, energy storage, peak-shaving and CO 2 capture with LNG/LO 2 cold energy utilization, which has remarkable features such as high efficiency, low first/operation/maintenance costs, zero CO 2 and NO x emission and massive off-peak power shifting. A calculation case is presented and the impacts of turbine inlet parameters, condensing pressure/condenser outlet temperature and feedwater temperature on the net electric efficiency excluding ASU and equivalent net electric efficiency as well as CO 2 capture features are analyzed. The steam content in vapor phase of the condenser outlet is considered which requires more cooling capacity for CO 2 capture. Under the conditions that the condenser outlet temperature/condensing pressure is 30 °C/30 kPa and feedwater temperature is 300 °C, with fully CO 2 capture, the net electric efficiency excluding ASU and equivalent net electric efficiency are 0.4386 and 0.4105 respectively with turbine inlet parameters of 600 °C/30 MPa, and they can reach 0.5327 and 0.5046 respectively with turbine inlet parameters of 1000 °C/40 MPa. [ABSTRACT FROM AUTHOR]

Inferior specific capacity and sluggish redox kinetics are the most stubborn problems lithium-ion and lithium-sulfur batteries (LIBs and LSBs) are facing, respectively. Here we report a facile fabrication of self-supported hollow Co 3 O 4 @carbon nanotubes on carbon cloth (H-Co 3 O 4 @CNT/CC) through a mild pyrolysis-oxidation process. The additive- and binder-free H-Co 3 O 4 @CNT/CC shows excellent electrochemical performances as both LIBs and LSBs electrodes. As a robust integrated anode for LIBs, the areal capacities are 2.72 mAh cm−2 at the current density of 0.5 C over 1000 cycles. While as a durable cathode host for LSBs, favorable areal capacities of 2.37 mAh cm−2 are maintained with a low capacity decay of 0.11 % per cycle at the sulfur loading of 6 mg cm−2 and current density of 1 C after 400 cycles. Electrochemical technology, ex situ Raman spectroscopy and DFT calculations are performed to comprehensively analyze H-Co 3 O 4 @CNT/CC via thermodynamics and kinetics. It is demonstrated that the hierarchically hollow interior structure, strong adsorb ability of Co 3 O 4 toward polysulfides and three-dimensional (3D) inter-connected conductive carbon framework are responsible for the high areal capacity, fast redox kinetics and cycling durability. [Display omitted] • The integrated electrode possesses the merits of hollow nanostructured Co 3 O 4 and 3D inter-connected conductive network. • Electrochemical technology and DFT calculations are performed to comprehensively analyze H-Co 3 O 4 @CNT/CC. • H-Co 3 O 4 @CNT/CC delivers high areal capacities of 2.72 mAh cm-2 after 1000 cycles at 0.5 C as anode. [ABSTRACT FROM AUTHOR]

Periodic pressure waves propagating in drilling fluids along the wellbore are widely used to transmit the downhole information through the drillstring. Although various evaluation models for the wellbore and periodic pipe flows have been studied in published literature, the influence of the frequency and multi-boundary conditions on these models for the non-Newtonian drilling fluid is rarely considered. The paper presents a one-dimensional equivalent model to simulate the propagation of the periodic pressure waves in drilling fluids along the wellbore based on the assumption that the system is isothermal and the internal diameter of drillstring is a constant value. Specially, the periodic pressure waves are divided into low-frequency part (such as pump-on pulse) and high-frequency part (such as pressure wave generated by mud pulse telemetry system). The interactions of these two parts with the turbulence and Bingham fluid are investigated based on the Navier–Stokes equation for a 2D axisymmetric transient flow subjected to the five boundary conditions including the pump, air chamber, mud pulse telemetry system, drill bit and the outlet. A finite difference method with second-order accuracy is used to solve the numerical model. Experiments in the shallow and deep wells are conducted to validate the model. The simulated results are in good agreement with the experiment measurement. Finally, the influence of the frequency on pressure wave attenuation is analyzed and the result is compared with those calculated from acoustic attenuation formula. Both results show consistent trend with increasing frequency. [ABSTRACT FROM AUTHOR]

The widely used fin-and-tube heat exchangers have a low air-side heat transfer capacity. Enhancing the air-side thermo-hydraulic performance is a key point of the relevant research. Vortex generators have been proven to be one of the most promising techniques to improve the air-side heat transfer capacity of the fin-and-tube heat exchangers. Herein, this paper proposed an original sinusoidal wavy winglet type vortex generator to achieve high heat transfer performance with moderate increased pressure drop penalty. A three-dimensional numerical simulation was conducted to explore the air-side thermo-hydraulic performance with Reynolds number ranging from 1027 to 2054. The longitudinal vortex is generated in the channel so as to enhance the intensify of convective heat transfer. Especially, the wave-shaped vortex generators can produce many local small-scale secondary flows. And it is confirmed that the frontal area of the vortex generator can be effectively extended by such wavy shape and a more intensified disturbance can be caused in the air-side. Furthermore, the effects of the attack angle (α), dimensionless height (H p) and especially arrange position of the vortex generator were investigated. Additionally, the ranges of the Nusselt number ratio, friction factor ratio and surafece goodness factor in this study are 1.09–1.52, 1.09–2.31, and 1.06–1.24, respectively. Moreover, it is also very crucial to evalute the grade of energy and to explore the irreversible loss druing the heat tranfer process in view of the second law of thermodynamics. And the thermal dissipation can be reduced by up to 5.85% compared with the plain fins from the perspective of exergy analysis. [ABSTRACT FROM AUTHOR]

In this work, we propose the using of a transient acoustic imaging technique to analyze blade-vortex interaction (BVI) noise, which is considered as one of the dominant noise sources from rotorcraft. A simplified but representative set-up with a two-bladed rotor in the presence of a moving flow is considered herein. First, we conducted a delayed detached-eddy simulation to reveal the associated flow physics and to identify the distinctive flow structures during the BVI process. The numerical analysis complements the physical understanding gained from the following acoustical imaging analysis, where a recently developed phase-averaged wavelet-based beamforming method in the time-frequency domain is adopted. Compared to transient flow structures, which have been visualized in the numerical study, the acoustic imaging results clearly demonstrate the transient analysis capability of the proposed approach. It is impossible to achieve such a transient analysis capability by simply using the classical beamforming method. In particular, the transient analysis shows that the dominant noise sources would move along the blade in the radial direction, by essentially following the corresponding BVI positions on the blade, which is also consistent with the numerical results. Overall, the proposed method can help achieve a deepened physical understanding of transient aerodynamic and aeroacoustic process and could find applications in low-noise rotorcraft designs. [ABSTRACT FROM AUTHOR]

Abstract: A visualization study is conducted to investigate condensation flow in wide rectangular silicon microchannels with the hydraulic diameter of 90.6 μm and width/depth ratio of 9.668. Droplet-annular compound flow, injection flow, and vapor slug-bubbly flow are observed along the channel, which differ from that in other cross-sectional shape microchannels. In the droplet-annular compound flow region, the vertical walls (short side) of the channel are completely covered by the condensate, while droplet condensation still exists on the horizontal wall (long side) of the channel. The location of the injection flow will be postponed with the increasing inlet vapor Reynolds number. The injection frequency will increase with the increasing inlet vapor Reynolds number and condensate Weber number. More specifically, the frequency in the wide rectangular microchannels is lower than that in triangular microchannels having the same hydraulic diameter. It is confirmed that the cross-sectional shape of the microchannel plays a significant role on the instability of condensation flow. In addition, the correlation of Nusselt number is also presented. [Copyright &y& Elsevier]

Abstract: A steady one-dimensional model for annular condensation flow in triangular microchannels is developed. The curvature radius distribution of the condensate stream along the channel has been determined numerically. The results indicate that the curvature radius of the liquid phase would increase rapidly at the beginning, and then as the condensation process progresses along the length of the microchannels, the radius increase would proceed more slowly. At the end of the condensation flow, the radius increases rapidly again. A smaller contact angle and heat flux or a larger hydraulic diameter and steam pressure will all result in a longer condensation length. [Copyright &y& Elsevier]

In this study, monotonic and reversed-cyclic loading tests were conducted on six diagonally reinforced cold-formed steel (CFS) shear walls sheathed with a gypsum board (GYP) and a magnesium crystal board (MCB), respectively, to evaluate the effects of sheathing panels and different types of diagonal bracings on the shear capacity, lateral stiffness, ductility, and energy dissipation capacity of CFS shear walls. The results revealed that the stiffness of the skeleton, the sheathing material, the performance of the screw connections, and the construction of the splice of the wall panels have a distinct effect on the shear performance of the wall. The cooperative work effect of the rigid and strap bracings was excellent, and the ultimate strength and lateral stiffness of the wall were effectively improved by using an extra steel strap bracing. The shear performance of the wall sheathed with the MCB was higher than that of the wall sheathed with the GYP. When a flat steel strap was used to connect the panel splices, the torsion of the flat steel strap reduced the overall performance of the wall panels. This should be considered in practical engineering applications. • Six full-scale CFS shear walls were tested under monotonic and cyclic load. • The cooperative work effect of rigid and strap bracings was excellent. • The mechanical properties of the wall sheathed with MCB were better. • The diagonal braceing should be strengthened in the joint area. [ABSTRACT FROM AUTHOR]

The feed water heaters in power plants are actually the condensers using turbine extracting steam to heat feed water. The vertical feed water heater occupies less area than the horizontal one and convenient to lift tube bundles out in maintenance. However, the lower heat transfer coefficient due to thick condensate film limits its application. A novel trisection helical baffled vertical condenser (feed water heater) is proposed with liquid dams and gaps for facilitating condensate drainage. The flow and condensation heat transfer characters of two vertical condensers with variable angled trisection helical baffles of both single-thread and dual-threads and a variable spanned segmental baffled one were numerically studied with Mixture model of Fluent software. The distributions of velocity, pressure, volume fraction of condensate, and local heat transfer coefficient in these heat exchangers were demonstrated. The simulation results show that the inclined baffles with liquid dam and drainage gaps could drain condensate effectively from tube bundle surfaces and prevent liquid film from entraining into vapor, and that the variable angled trisection helical baffled vertical condenser with dual-threads could greatly improve the condensation heat transfer coefficient up to 35.7% higher than that of the variable spanned segmental baffled one. [ABSTRACT FROM AUTHOR]

• The power plant feedwater heaters and the countercurrent U-tube heat exchangers all involve half-cylindrical shell space. • Half-cylindrical space heat exchangers with ladder helical, orifice and segmental baffles were experimentally investigated. • The ladder helical baffle scheme has superior heat transfer coefficient and comprehensive index than those of the other ones. • The orifice baffle scheme has higher comprehensive index but lower heat transfer coefficient than those of segmental ones. • The average values of h o Δ p o −1/3 of ladder helical and orifice baffle schemes are about 15% higher than that of segmental one. The superheated steam cooling section and the condensate cooling section of the power plant feedwater heaters and the countercurrent U-tube heat exchangers all involve heat transfer in half-cylindrical shell space. The overall and shell-side heat transfer coefficients (h.t.cs.), pressure drop, and the comprehensive performances of some half-cylindrical space heat exchangers with different baffle structures were experimentally investigated. The investigated structures include three ladder helical baffle types [single inclined ladder helical (SH), dual inclined ladder helical (DH) and folded ladder helical (FH)], three orifice baffle types [fillet triangle orifice (F), trefoil-orifice (T) and quatrefoil-orifice (Q)], and segmental baffles (S), and all schemes are of two baffle pitches. Under the same baffle pitch and working condition, the experimental results show that the shell-side h.t.cs. of the ladder helical baffle schemes are higher than those of the orifice baffle schemes and segmental baffle ones; and the shell-side pressure drops of the orifice baffle schemes are much lower than those of the ladder helical baffle schemes and the segmental ones. The values of average comprehensive index h o Δ p o −1/3 of the ladder helical schemes FH-40, DH-40 and the orifice baffle schemes F-40 and T-40 are respectively 14.26%, 17.58%, 15.62% and 12.82% higher than that of the segmental scheme S-40. [ABSTRACT FROM AUTHOR]

• A novel helical baffle with small inclined angle and folded structure is proposed. • The new helical baffles can be created by cheap 2D laser cutting and folding. • The leakage between two folded helical baffles can be greatly decreased. • The novel electric heaters have excellent flow and heat transfer performances. • Folded helical baffles are more excellent at large equivalent angles in this work. The difficult manufacturing of helical baffles hinders the widespread application of the enhancement technology and the shortcut leakage between adjacent baffles impairs the enhancement effects. To solve these two issues, the promising anti-leakage and easy-to-manufacture helical baffles with small inclined angle and folded structure are proposed, which can be produced by 2D laser cutting and simple mechanical folding. The influence of different helical baffle configurations, including three normal helical schemes, three axial separation helical schemes, three novel folded axial separation helical baffle schemes and a segmental scheme on the performance of electric heaters are numerically investigated. The equivalent angles of helical schemes adopted in this work are 15°, 20° and 25°, and the inclined angle of helical baffles under axial separation connection style is 10°. Compared with the corresponding axial separation scheme without folding, the leakage can be significantly decreased, the heat transfer coefficients h and the comprehensive indices h ⋅Δ p −1/3 of FH15(10)°, FH20(10)° and FH25(10)° are increased by 6.5%/2.3%, 12.2%/7.3% and 20.4%/13.0%, and the averaged tube wall temperatures T w are decreased by 12.5 K, 25.4 K and 54.7 K, respectively. This research can provide feasibility for the extended application of helical baffles in electric heaters or heat exchangers. [ABSTRACT FROM AUTHOR]

• A novel square-tube-layout coupling-vortex scheme is proposed in TETHX. • More uniform temperature fields are observed in coupling-vortex schemes. • Nu, f reduce but Nu∙f −1/3 rises with rising S , but all increase with rising A / B. • The smaller S and the closer A / B is to 1, the more obvious advantage of TETHX-CV. • Nu / f / Nu ∙ f −1/3 of C12.3S50 are 12.8%/15.2%/7.6% higher than those of P12.3S50. The twisted elliptical tube heat exchangers with the novel coupling-vortex chessboard tube layout (TETHXs-CV) were simulated with the RNG k - ε model in software Fluent 15.0. The shell-side flow pattern at the tangential points between adjacent tubes in traditional TETHX is countercurrent while that in TETHX-CV is concurrent, which helps enhance heat transfer capability without any extra manufacturing cost. The impacts of the ratio A / B of the major axis to the minor axis and the twist pitch S were also investigated. The results indicate that with the increase of A / B and the decrease of S , the secondary flow behaves more intensely, the Nusselt number Nu and the friction factor f increase, while with the increase of A / B and S , the comprehensive evaluation index Nu∙f −1/3 increases. The Nu, f and Nu ∙ f −1/3 of all twisted tube schemes are higher than those of the smooth round tube schemes R10.8. Compared with corresponding parallel-vortex schemes, the coupling-vortex schemes possess more uniform temperature fields, and the average Nu, f and Nu ∙ f −1/3 of the coupling-vortex schemes C12.3S50/C12.3S100 increase by 12.8%/9.9%, 15.2%/10.5% and 7.6%/6.3%, respectively; the smaller S or the closer A / B is to 1, the more advantageous the TETHX-CV. [ABSTRACT FROM AUTHOR]

Hollow multicomponent transition metal oxide nanostructures have caused extensive attention due to their enhanced performances in lithium-ion batteries (LIBs). Herein, a hybrid of multicomponent 3NiO·2Ni 3/2 Co 1/2 ZnO 4 nanocomposite with porous hollow dodecahedron nanostructures (3NiO·2Ni 3/2 Co 1/2 ZnO 4 -HD) was fabricated by carbonization of NiCoZn-layered double hydroxides which were derived from multimetallic zeolitic imidazolate frameworks (Zn/Co-ZIFs) as both self-sacrificial template and precursors. The 3NiO·2Ni 3/2 Co 1/2 ZnO 4 -HD nanocomposites were carefully characterized by various techniques including scanning electron microscopy, X-ray powder diffraction, X-ray photoelectron spectroscopy, thermogravimetric analysis, N 2 adsorption/desorption, transmission electron microscopy, Four-Point Probes and electrochemical techniques. When the 3NiO·2Ni 3/2 Co 1/2 ZnO 4 -HD nanocomposites were acted as anode materials for LIBs, a capacity of about 1337 mA h g −1 could be obtained after 100 cycles. The improved electrochemical performances might originate from synergistic effect of multicomponents, enhanced electrical conductivity and porous hollow dodecahedron nanostructures which could effectively alleviate volume deformation in the process of discharge/charge, accelerate mass transfer and increase the active sites for Li + storage. [ABSTRACT FROM AUTHOR]

Abstract: A three-dimensional model of heat transfer and fluid flow in noncircular microchannel heat sinks is developed and analyzed numerically. It is found that Nusselt number has a much higher value at the inlet region, but quickly approaches the constant fully developed value. The temperature in both solid and fluid increases along the flow direction. In addition, the comparison of thermal efficiencies is conducted among triangular, rectangular and trapezoidal microchannels. The result indicates that the triangular microchannel has the highest thermal efficiency. [Copyright &y& Elsevier]

Abstract: A visualization experiment is conducted to investigate the condensation of steam in a series of triangular silicon microchannels. The results indicate that droplet, annular, injection and slug-bubbly flow are the dominant flow patterns in these triangular silicon microchannels. With increased mass flow rate, or an increase in the hydraulic diameter under the same Reynolds number, the location at which the injection occurred is observed to move towards the channel outlet. The frequency of the injection increases, i.e. the flow of condensation instability is higher with increased inlet vapor Reynolds number, condensate Weber number and the prolongation of the injection location, or with a decrease in the hydraulic diameter of the channel. In addition, the wall temperature of the channel decreases along the condensation stream. The total pressure drop, the average condensation heat transfer coefficient and the average Nusselt number are observed to be larger with increased inlet vapor Reynolds number. Moreover, it is found that the condensation heat transfer is enhanced by a reduction in the channel scale. [Copyright &y& Elsevier]

Abstract: A theoretical model of fluid flow and heat transfer in a heat pipe with axial “Ω”-shaped grooves has been conducted to study the maximum heat transport capability of these types of heat pipes. The influence of variations in the capillary radius, liquid–vapor interfacial shear stress and the contact angle are all considered and analyzed. The effect of vapor core and wick structure on the fluid flow characteristics and the effect of the heat load on the capillary radius at the evaporator end cap, as well as the effect of the wick structure on the heat transfer performance are all analyzed numerically and discussed. The axial distribution of the capillary radius, fluid pressure and mean velocity are obtained. In addition, the calculated maximum heat transport capability of the heat pipe at different working temperatures is compared with that obtained from a traditional capillary pressure balance model, in which the interfacial shear stress is neglected. The accuracy of the present model is verified by experimental data obtained in this paper. [Copyright &y& Elsevier]

• Coupling-vortex triangular tube layout is proposed without extra manufacturing cost. • Concurrent flow, larger A / B and smaller S cause stronger secondary flow. • The Nu and Nu · f −1/3 of C14.2S50 is 132.8% and 47.1% higher than R10.8. • Smaller S and smaller A / B lead to greater advantage of TETHXs-AVRCV. • The averaged Nu / Nu · f −1/3 of C12.3S50 are 7.8%/4.9% higher than those of P12.3S50. An innovative alternating V-rows triangular tube layout was devised for the twisted elliptical tube heat exchangers to enhance heat transfer between adjacent tubes. Under the same tube circumference, altogether eleven twisted elliptical tube heat exchangers with two tube layouts, diverse aspect ratios of twisted elliptical tubes and different twisted pitches were constructed and simulated, including five coupling-vortex schemes, five parallel-vortex schemes and a smooth round tube scheme R10.8. Water with constant physical properties was adopted as the working fluid. Shell-side Reynolds number varies from 2000 to 10,000. The results show that the concurrent flow and the irregular channel in coupling-vortex schemes, and the larger aspect ratio and the smaller twisted pitch of twisted elliptical tubes help intensify turbulence and secondary flow. Compared with R10.8, the averaged Nu and Nu · f −1/3 of coupling-vortex scheme C14.2S50 are improved by 132.8% and 47.1%, respectively. Under shorter twisted pitch, smaller aspect ratio and lower Reynolds number, coupling-vortex schemes can acquire superior heat transfer capability than corresponding parallel-vortex schemes but will not increase manufacturing cost. Compared with P12.3S50, the maximum and averaged Nu of C12.3S50 are increased by 9.5% and 7.8% while the maximum and averaged Nu · f −1/3 are increased by 6.4% and 4.9%. [ABSTRACT FROM AUTHOR]