Spouted bed electrowinning of zinc: Part II. Investigations of the dynamics of particles in large thin spouted beds

The behavior of particles in thin spouted beds, mostly equipped with draft tubes, has been investigated. Three apparatuses have been used: a laboratory-scale cylindrical bed, a 2-m-tall “flat” (rectangular cross section) bed and a 2-m-wide flat bed, the last equipped with multiple draft tubes. Most of the results were obtained on the tall bed. Minimum spouting flow rate, pressure distribution, particle velocities, and solid circulation rates were determined as a function of bed geometry (including draft tube dimensions and position). Observations were made of the direction of liquid flow in the bed outside the draft tube and of the occurrence of zones in the bed where the particles appeared stationary. The wide bed was used to determine that there is a maximum separation between draft tubes beyond which particles cannot be kept in motion across the whole width of the bed.     

Blast furnace circumferential process symmetry: effect of flow distribution in hot blast systems

Abstract

Solid particle flow patterns in the moving bed zone of a melter/gasifier were studied using discrete element method (DEM). Interparticle forces were calculated using the Hertz–Mindlin no slip contact model. The simulation results of the solid particle flow patterns agree well with the experimental results exhibited by tracer particles. The solid particle flow pattern and descending velocity were studied, as well as the effect of the discharge rate of solid particles in the raceway on solid particle flow pattern in the moving bed.

Results show that the moving bed could be divided into four subdomains based on the velocity of solid particles. A stagnation zone with semielliptic geometry is formed at the central bottom of the moving bed during drainage of solid particles. Furthermore, the simulated results of compressive force among solid particles in the moving bed zone indicate that the deadman zone undergoes a high degree of compressive force, especially at the centre of the gasifier. This finding implies that more compressive force resistant solid material should be placed at the centre zone by manipulating solid particles fed into the melter/gasifier.     

A fundamental study of raceway size in two dimensions

Blast furnace raceway zones are formed by the force of the air blast injected through the tuyeres evacuating a region of the packed bed directly in front of these tuyeres. Raceway depths in blast furnaces have been historically predicted through the use of empirical correlations based on measurements on cold and hot models. These correlations are not found to be universal in application, however, with many researchers finding only fair agreement between their experi-mental data and the correlations proposed by other researchers. We present here an alternative physical mechanism approach for raceway formation based on examination of the fundamental properties of the system. The study includes two-dimensional experiments where raceway depths and shapes are measured and an accompanying theoretical and numerical analysis of the under-lying mechanisms. Gas flow distributions around the raceway zone are also examined. It is found that the raceway size for given blast conditions and particle properties is such that the total gas drag on the solids vertically above the raceway balances the solid bed weight, with some allowance for solid holdup by walls. The formulation of this theory leads to the further conclusion that the total surface area of the raceway walls as a fraction of the horizontal cross-sectional area of the container or furnace is a unique function of three factors: (a) the gas flow rate as a fraction of the gas flow rate required to fluidize the bed, (b) a particle Reynolds number calculated at the particle's incipient fluidization velocity, and (c) the shape of the horizontal cross section of the bed.     

Reaction rates for sulfur fixation with iron at 1100 to 1275 K

The rates of sulfidizing iron in a simulated coal gasification atmosphere were studied. Mixtures of H₂S and CO were passed through fixed beds of coal char and prereduced iron ore, and effluent gas compositions were measured as a function of time. These mixtures ranged from 2.5 pct to 10 pct H₂S at various flow rates, with temperatures from 1100 K to 1275 K and iron ore sizes from 10 mesh down to 100 mesh. Experimental conditions were established to form a steady state reaction profile in the fixed bed. Analysis of the exit gas provided a measurement of the profile. The slope of the profile was used directly as a measure of the reactivity of the solids in the bed. The development of this experimental technique and its experimental design requirements are discussed. The observed sulfidization rate of thein situ reduced iron ore is characterized by a single rate constantm (minutes^-1), which varies primarily with temperature and particle size and is substantially independent of gas flow rate, bed configuration, and H₂S content of the incoming gas. Accordingly, the rate constant m can be applied in the design of a combined sulfur fixation, coal gasification reactor to estimate the solids retention time, and the minimum mass of iron required per cross sectional area of reactor. CRAIG B. SHUMAKER, formerly a Graduate Student in the School of Materials Engineering, Purdue University     

Wall-to-bed heat transfer in a circulating fluidized bed for the reduction of iron ore particles

A model is presented that describes the wall-to-bed heat transfer in a circulating fluidized bed (CFB) used for the prereduction of iron ore in the smelting-reduction iron-making process. The model incorporates the core-annulus type flow structure and the wall emulsion layer growing downward along the surface. Model predictions showed good agreements with measured data taken from the literature. The hydrodynamic behavior near the wall surface was able to be properly described by the core-annulus flow structure. A higher heat-transfer coefficient with higher solid circulation flux was obtained in the upper part of the bed because of the heat input caused by the lateral diffusion of particles from the core. The predicted and measured data also showed the minima in the heat-transfer coefficients in the lower part of the bed. Model predictions indicated that in the CFB for the reduction of iron ore particles, it is important to properly control the inlet temperature of the reducing gas, rather than that of the solid particles. The implications of the behavior of heat transfer in the CFB are discussed for the reduction of iron oxides.     

Particle Densimetric Froude Number for Estimating Sediment Transport

It has been established that for ratios of flow depth to bed particle diameter less than ten (flow on very rough boundaries) neither the Reynolds number of the solid loose particles at a stream bed nor the Shields parameter are adequate variables to predict critical flow conditions for the initiation of motion. A particle densimetric Froude number F? = U/[(s?1)gD]1/2 (where U=mean velocity, s=ratio of sediment and fluid densities, g=acceleration due to gravity, and D=characteristic diameter of bed particle) is here proposed as an alternative criterion to predict hydraulic conditions for the initiation of motion. Values of critical F? were computed after calibration with available experimental data sets. After the critical conditions for the initiation of particle motion were exceeded, transport of bed particles was established. In order to evaluate the performance of a transport equation that contains F? in sediment transport, a set of the most employed formulations to estimate bed material transport in steep slope macrorough flows were tested. The comparison of the results shows that F? can be used to accurately predict sediment discharge.     

三杆式切断蝶阀的设计与开发

介绍了三杆式切断蝶阀的工作原理,并对世林(漯河)冶金设备有限公司研制开发的三杆式切断蝶阀结构形式、性能与特点做了详细分析。     

蝶阀在高炉热风炉系统的应用

对蝶阀在高炉热风炉系统的使用进行了阐述，并分析了各种蝶阀的优缺点、结构性能、工作原理及各种蝶阀的应用范围。     

Straight Benthic Flow-Through Flume for In Situ Measurement of Cohesive Sediment Dynamics

The design of a straight benthic flow-through flume for in situ studies of cohesive sediment dynamics is described including the flume structure and probes installed for routine measurements of suspended sediments and flow velocity. The flume was calibrated for two roughness types covering the range of possible cohesive bed roughnesses. The calibration included a set of three-dimensional velocity measurements using acoustic Doppler velocimeter. These measurements were used to develop calibration relationships between the bed shear stress (which is difficult to measure directly in routine deployments) and the flume centerline flow velocity, which is routinely measured. An example of a successful deployment of the flume is presented. The limitations and potential for further improvements are also briefly discussed.     

Citation impact, acceptance rate, and APA journals.

Investigated the role that factors such as journal circulation and acceptance rate play in relation to citation impact (CTI). CTI was negatively related to acceptance rate and positively related to circulation, consistent with the construct of CTI as a measure of journal quality. CTI was highest for moderate publication lag and had substantial stability over time. Compared to non-American Psychological Association (APA) journals, APA journals had significantly higher CTI in both 1977 and 1978, higher circulation, and lower acceptance rates. CTI is probably the best single measure of journal quality currently available. (PsycINFO Database Record (c) 2010 APA, all rights reserved)     

Heat transfer in a direct-fired rotary kiln: II. Heat flow results and their interpretation

Heat flow rates from the gas to the wall and to the bed have been derived from temperature profiles measured in the UBC pilot rotary kiln. The experimental gas-to-wall heat flux has been found to agree closely with theoretical predictions based on a simple radiative model consisting of a grey gas surrounded by a grey surface at uniform temperature. Under identical conditions, the gas-to-solids heat flux is up to ten fold greater than the heat flux between the gas and wall. The gas-to-solids heat flux is a function of the solids feed rate at low throughputs but is constant at higher throughputs. At the lowest feed rates and corresponding rotation speeds heat flow to the bed is limited by mixing of the solids. Heat transfer control changes to the gas side of the bed at higher feed rates and rotation speeds. Under the latter conditions convection appears to account for the major fraction of heat flow to the bed. The heat flow measurements relate directly to observations of the bed motion which can be conveniently characterized by a “bed behavior” diagram. The low heat flux to the bed at low feed rates is due to a slumping action at the surface and concomitant poor mixing. The high heat flux obtained at high feed rates coincides with the observation of a rolling bed. Burden-side and gas-side convective heat transfer coefficients, calculated from the heat flux data, have values ranging from 700 to 1200 and 120 to 240 w/m²K respectively.     

Numerical Modeling of Bed Evolution in Channel Bends

A two-dimensional numerical model is developed to predict the time variation of bed deformation in alluvial channel bends. In this model, the depth-averaged unsteady water flow equations along with the sediment continuity equation are solved by using the Beam and Warming alternating-direction implicit scheme. Unlike the present models based on Cartesian or cylindrical coordinate systems and steady flow equations, a body-fitted coordinate system and unsteady flow equations are used so that unsteady effects and natural channels may be modeled accurately. The effective stresses associated with the flow equations are modeled by using a constant eddy-viscosity approach. This study is restricted to beds of uniform particles, i.e., armoring and grain-sorting effects are neglected. To verify the model, the computed results are compared with the data measured in 140° and 180° curved laboratory flumes with straight reaches up- and downstream of the bend. The model predictions agree better with the measured data than those obtained by previous numerical models. The model is used to investigate the process of evolution and stability of bed deformation in circular bends.     

蝶阀轴端密封的研究

介绍了蝶阀类产品双组多层次轴端密封的结构及密封原理,以及应用该结构的注意事项.该结构在蝶阀设计中得到了广泛应用,并获得了国家实用新型专利(专利号:ZL 201120003939.5).     

Baroreflex control of coronary blood flow varies regionally in awake dogs

1. Baroreflex responses to changes in aortic pressure were measured simultaneously in three main coronary regions of awake dogs. 2. Pulsed Doppler flow probes were mounted at prior surgery on the right, circumflex and anterior descending coronary arteries; the animals were placed in complete heart block and the left ventricle was paced. After 2-4 weeks recovery, baroreflexes were evoked by inflating a balloon catheter placed in the mid-thoracic aorta via the femoral arteriotomy. Flow and pressure data were collected at rest, and during acute (8s) and steady-state (25s) baroreflex challenge. 3. Changing ventricular rate alone caused a fall in aortic pressure at low rates; however, over the range 60 to 180 b.p.m., circumflex and anterior descending coronary flow and conductance changed directly with ventricular rate, but right coronary flow and conductance remained unchanged. 4. Acute aortic pressure elevation increased flow at 8s in all beds at all rates. Conductance effects at 60 b.p.m. were negligible in all three beds, but rose at 100 and 180 b.p.m. in the right and circumflex beds. 5. Sustained aortic pressure elevation (25s) caused flow to return towards control in all beds ventricular rates, but in the right coronary at 60 b.p.m. flow fell below control. Conductance at this time was unchanged at all rates in the anterior descending bed, fell modestly in the circumflex, and decreased to below resting in the right coronary bed. 6. Baroreflex control of coronary flow and conductance thus varies between territories, and within territories, depending on ventricular rate. The right coronary bed appears to be regulated by a bidirectional, baroreflex-linked mechanism, which is functionally opposite in action to that found in most vascular beds.     

Pulmonary capillary pressure and tissue perfusion: clinical implications during resuscitation from shock

During shock resuscitation, a combination of fluids, vasopressors, vasodilators, and inotropes is administered in order to achieve a cardiac output or overall oxygen delivery as per guidelines of individual clinicians. The measurement of ventricular end-diastolic pressure allows a clinician to describe a therapeutic goal of optimum cardiac output response to changes in end-diastolic pressure. This concept has formed the backbone of resuscitative strategies in many forms of shock. Ventricular end-diastolic pressure is indirectly measured as the pulmonary artery occlusion pressure (PAOP) in critically ill patients with the use of a pulmonary artery catheter. Cytokines and other mediators may injure the pulmonary capillary endothelium which will affect the rate of leakage in the pulmonary capillaries. This may have important clinical implications in the therapy of shock in inflammatory states such as sepsis and the adult respiratory distress syndrome. Therefore, the true edema-forming pressure within the pulmonary bed is of considerable importance to the intensivist at the bedside. True pulmonary capillary pressure represents the midpoint of the capillary bed and is the hydrostatic pressure which directly drives the rate of pulmonary interstitial edema formation. During shock resuscitation in disorders in which vascular integrity may be impaired, the ability to measure pulmonary capillary pressure would be of great clinical benefit. It is impossible to directly measure pulmonary capillary hydrostatic pressure in the intact lung and, therefore, only indirect measurements are clinically possible. Numerous studies have demonstrated the lack of consistent relationship between the pulmonary capillary pressure, PAOP, pulmonary artery diastolic pressure, and the severity of acute lung injury. The assumption that PAOP, and thus left atrial pressure, is a good indirect measurement of pulmonary filtration pressure within the capillary bed is erroneous, in particular in the presence of increased resistance within the pulmonary venous bed between the capillaries and the left atrium, as may exist in disorders in which there is cytokine production. It is now clear that a significant gradient between pulmonary capillary pressure and PAOP may be present in inflammatory disorders which are not present in noninflammatory states, and that pulmonary capillary pressure may be measured at the bedside of critically ill patients. Bedside measurement of pulmonary capillary pressure may allow for added precision in our therapeutic goals in resuscitation from inflammatory shock. If further studies confirm the reliability and reproducibility of bedside measurement, pulmonary capillary pressure may become an invaluable part of the hemodynamic profile in the critically ill patient in shock.     

Sand Transport in Nile River, Egypt

Measurements of bed-load and suspended-load transport rates were carried out successfully at four cross sections of the Nile River, in Egypt, along the entire length from Aswan to Cairo using a mechanical sampler called the Delft Nile Sampler. The measured transport rates were compared to similar data sets from two other large scale rivers: the Rhine-Waal River in the Netherlands and the Mississippi River in the USA. The bed-load transport rates in the Nile River and in the Rhine-Waal River are in very good agreement. Comparison of suspended transport rates in the Nile River and in the Mississippi River shows that both data sets are complementary, revealing a very consistent trend of suspended transport against current velocity; suspended transport is roughly proportional to (Vav)3?to?4. Three formulas for the prediction of bed-load transport were tested using the Nile data: Meyer-Peter–Muller, Bagnold, and Van Rijn. The prediction formula of Van Rijn produced significantly better results than the other two formulas; the average relative error was about 60%. The formula of Van Rijn was modified to extend it to conditions with slightly nonuniform sediment mixtures by introducing a correction factor for the bed shear parameter. Based on a limited number of flume experiments, the correction factor was found to be dependent on the characteristics of the sediment mixture (d10, d50, d90, and σg). Comparison of bed-load transport measured in the Nile River with computed transport rates of the modified formula showed improved results; the average relative error decreased to about 30%. The formulas of Bagnold and Van Rijn were also used to compute the suspended transport rates in the Nile River. The computed transport rates were found to be within a factor of 2 of measured values; the formula of Bagnold performed slightly better. The total load transport formula of Engelund–Hansen was also successfully used (computed values within a factor of about 2 of measured values).     

一种新型双位蝶阀的研制及在台车式热处理炉的应用

通过一种新型双位蝶阀的研制和使用,解决了热处理炉大小火调节的问题,并且提高了双位蝶阀的可靠性和使用寿命,大大提高了火焰式台车热处理炉的炉温控制稳定性和使用寿命。     

Modelling Effect of Circulation Flow Rate on Inclusion Removal in RH Degasser

Based on the similarity principles,a 1∶ 7 scale physical model was established to study the behavior of molten steel flow and inclusion removal in a 145 t Rheinsahl-Heraeus( RH) degasser.On the basis of the quantitative measurements of the circulation flow rate and inclusion removal under various lifting gas flow rates,the effect of circulation flow rate on inclusion removal was investigated in the RH degasser.The inclusion removal rate shows the trend of first increase and then decrease twice with increasing the circulation flow rate when the circulation flow rates are smaller than 104.7 L/min.Whereas,the inclusion removal rate increases again with the further increase in circulation flow rate when the circulation flow rate is larger than 104.7 L/min.At lower circulation flow rates,inclusions are mainly removed by Stokes flotation to the slag/steel interface after inclusions are transferred near the slag/steel interface by the circulation flow.At higher circulation flow rates,the collision and aggregation of inclusions improves the inclusion removal efficiency.With the further increase in the circulation flow rate,inclusions are mainly removed by following the turbulent fluctuation( turbulent diffusion)to the slag/steel interface after inclusions are transferred near the slag/steel interface by the circulation flow.     

Application of simplified rapid equilibrium models in simulating experimental breakthrough curves from fixed bed biosorption reactors

A modelling approach for a fixed bed biosorption column is presented. The Advection–Dispersion–Reaction (ADR) equation has been applied as the basic modelling equation for the special case of Local Equilibrium (LE). The model implements the minimum parameters for describing a fixed bed biosorption column, employing the geometrical dimensions of the bed, the packing arrangement, the operating conditions of the system, and the sorptive characteristics of the biosorbent material. An apparent axial dispersion coefficient has been used as a key parameter of the model. The authors compare model predictions to selected examples of experimental biosorption breakthrough curves reported from pilot scale work. Although the main assumption of the model is that biosorption equilibrium is rapid, the use of an apparent overall dispersion coefficient makes the model applicable for the cases where mass transfer resistances are present in the liquid and solid phases.