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Potential of Biogas Production from Anaerobic Co-digestion of Hydrothermal Pre-treated OPEFB and Digested Sludge 厌氧协同消化经热预处理的 OPEFB 和消化污泥产生沼气的潜力
Q3 Chemical Engineering Pub Date : 2024-05-17 DOI: 10.37934/arfmts.117.1.155163
Muhammad Bukhari Rosly, Pramila Tamunaidu, Nurhamieza Md Huzir, Azlan Nur Rasyid Amin, Masafumi Goto, Abd Halim Md Ali, Mohd Danial Muhd Ali
The palm oil industry plays a vital role in Malaysia, but it generates substantial amounts of biomass waste, which, if not properly managed, can lead to environmental pollution. Among these waste products, oil palm empty fruit bunch (OPEFB) is the most abundant and underutilized, being generated daily without any commercial value. The aim is to efficiently convert OPEFB into fermentable sugars for improved biogas production. Nevertheless, the challenge lies in efficiently degrading OPEFB within a short timeframe before fermentation into biogas can occur. This study aims to explore the potential of hydrothermal pre-treatment as a means to enhance biogas production from OPEFB. The pre-treatment process was optimized by varying reaction temperatures (100 to 250°C), and reaction times (10 to 40 minutes). The main objective was to maximize the total soluble sugar yield, a crucial precursor for efficient biogas production. The optimal conditions for hydrothermal pre-treatment are identified at a temperature of 175°C and a reaction time of 20 minutes, resulting in a yield of 49.2 mg of glucose per gram of OPEFB. Subsequent anaerobic co-digestion of the treated OPEFB with digested sludge increased methane yield to 100.53 ml/g-VS, representing a remarkable 392% increase compared to the low 20.44 ml/g-VS produced by untreated OPEFB. Nonetheless, elevated pre-treatment temperatures (200°C and above) led to reduced biogas production due to inhibitory compounds. This study demonstrates the effectiveness of hydrothermal pre-treatment as a low-temperature, green technology for enhancing OPEFB-based biogas production, contributing to Malaysia's renewable energy goals. Future research should focus on scale-up and validation of this integrated process.
棕榈油产业在马来西亚发挥着重要作用,但它会产生大量的生物质废物,如果管理不当,会导致环境污染。在这些废弃物中,油棕空果束(OPEFB)的数量最多,但利用率却很低,每天都在产生,没有任何商业价值。我们的目标是将油棕空果束有效转化为可发酵糖,以提高沼气产量。然而,在发酵成沼气之前,如何在短时间内有效降解 OPEFB 是一项挑战。本研究旨在探索水热预处理作为提高 OPEFB 沼气产量的一种手段的潜力。通过改变反应温度(100 至 250°C)和反应时间(10 至 40 分钟)对预处理过程进行了优化。主要目的是最大限度地提高可溶性糖的总产量,这是高效生产沼气的关键前体物。水热预处理的最佳条件是温度为 175°C,反应时间为 20 分钟,从而使每克 OPEFB 的葡萄糖产量达到 49.2 毫克。随后,经处理的 OPEFB 与消化污泥进行厌氧共同消化,甲烷产量增至 100.53 毫升/克-VS,与未经处理的 OPEFB 产生的 20.44 毫升/克-VS 相比,显著增加了 392%。然而,由于抑制性化合物的存在,预处理温度升高(200°C 及以上)导致沼气产量减少。这项研究证明了水热预处理作为一种低温绿色技术在提高 OPEFB 沼气产量方面的有效性,有助于实现马来西亚的可再生能源目标。未来的研究应侧重于这一综合工艺的放大和验证。
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引用次数: 0
Feasibility of Electric Fishing Boats based on Evaluation of Hydrostatic Forces and Resistance 根据静水压力和阻力评估电动渔船的可行性
Q3 Chemical Engineering Pub Date : 2024-05-04 DOI: 10.37934/arfmts.116.2.7587
Ahmad Ilham Ramadhani
Conventional gasoline engine fishing boats have several disadvantages, such as high exhaust emissions, high fuel consumption, and low service life. The disadvantages of the gasoline engine can be resolved by using the electrical engine. Electrical fishing boats is an improvement on conventional boat to reduce the fuel consumption and emissions. In realizing an electric fishing boat, a feasibility analysis of the design, shape and weight that can be accommodated is required. The feasibility of an electric fishing boat has been successfully carried out by simulating the boat on Maxsurf Software. The aim of this research is to analyze feasibility of conventional boats by designing electric fishing boats. Improving feasibility is carried out by calculating hydrostatic forces and resistance. Electric fishing boats design using the simulation model in Maxsurf Modeller and simulation of resistance in Maxsurf Resistance at speeds of 1, 3 and 5 knots, with Wyman method. The modeling results show that the electric fishing boat design has a pointed front configuration with a V-shaped bottom. Main dimensions LoA 3.49 m, width 0.8 m; height 0.5 m; and a draft of 0.2 m, the boat produces a hydrostatic force which includes a displacement of 301.5 kg, a midship draft and submerged area of 0.2 m, a wet area of 3.08 m2, and a waterline of 0.5 – 1.5 m. Testing 1, 3, and 5 knots, the boat experienced resistance of 26.11 N, 234.96 N, and 652.73 N respectively. The power required for the boat to operate was 13,43 W, 362.66 W, and 1678,97 W. The feasibility of designing an electric fishing boat is the main key to developing an electric fishing boat.
传统的汽油发动机渔船有几个缺点,如废气排放量大、油耗高和使用寿命低。使用电力发动机可以解决汽油发动机的缺点。电动渔船是对传统渔船的改进,可降低油耗和排放。在实现电动渔船的过程中,需要对设计、形状和可容纳的重量进行可行性分析。通过在 Maxsurf 软件上对电动渔船进行模拟,已经成功地进行了可行性分析。这项研究的目的是通过设计电动渔船来分析传统渔船的可行性。通过计算静水压力和阻力来提高可行性。使用 Maxsurf Modeller 中的仿真模型和 Maxsurf Resistance 中的阻力仿真来设计电动渔船,速度分别为 1、3 和 5 海里,采用 Wyman 方法。建模结果表明,电动渔船的设计采用前尖后底的 V 形结构。主要尺寸为 LoA 3.49 米、宽 0.8 米、高 0.5 米、吃水 0.2 米,该船产生的静水压力包括排水量 301.5 千克、舯吃水和水下面积 0.2 米、湿面积 3.08 平方米、水线 0.5 - 1.5 米。在测试 1、3 和 5 海里的速度时,该船的阻力分别为 26.11 牛、234.96 牛和 652.73 牛。渔船运行所需的功率分别为 13.43 瓦、362.66 瓦和 1678.97 瓦。设计电动渔船的可行性是开发电动渔船的主要关键。
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引用次数: 0
Unsteady Flow of Hybrid Nanofluids Subjected to a Stretching/Shrinking Sheet with Heat Generation 受拉伸/收缩片影响的混合纳米流体的非稳态流动与热量产生
Q3 Chemical Engineering Pub Date : 2024-05-04 DOI: 10.37934/arfmts.116.2.5974
Noorina Abdul Rahman, Najiyah Safwa Khashi’ie, Iskandar Waini, Khairum Hamzah, Mohd Afzanizam Mohd Rosli, Ioan Pop
This work highlights the thermal progress and flow characteristics of the various hybrid nanofluids (graphene-alumina/water and copper-alumina/water) flow over a stretching/shrinking sheet with heat generation and suction effects using numerical approach. This study is important in identifying the nanofluids and physical parameters which beneficial in the increment of the flow and thermal progresses. The control model (partial differential equations) is established based on the boundary layer assumptions and then transformed into a set of ordinary (similar) differential equations. A numerical solver in the MATLAB software called the bvp4c solver is used to compute the solutions by first transforming the reduced ODEs. There is an increase in velocity profile and a decrease in thermal rate with the increased suction parameter. It is observed that between the two hybrid nanofluids, the Cu-Al2O3/H2O hybrid nanofluid has a larger thermal rate and skin friction coefficient compared to the Graphene-Al2O3/H2O, which makes Cu-Al2O3/H2O a good option for the industrial cooling processes.
本研究采用数值方法,重点研究了各种混合纳米流体(石墨烯-氧化铝/水和铜-氧化铝/水)在拉伸/收缩片上流动时的热量产生和吸力效应,以及流动特性。这项研究对于确定纳米流体和物理参数非常重要,这些参数有利于流动和热量的增加。控制模型(偏微分方程)是根据边界层假设建立的,然后转化为一组常(相似)微分方程。在 MATLAB 软件中使用名为 bvp4c 求解器的数值求解器,通过首先转换简化的 ODE 来计算解。随着吸力参数的增加,速度剖面增大,热率降低。据观察,在两种混合纳米流体中,与石墨烯-Al2O3/H2O 相比,Cu-Al2O3/H2O 混合纳米流体的热速率和皮肤摩擦系数更大,这使得 Cu-Al2O3/H2O 成为工业冷却过程的良好选择。
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引用次数: 0
Innovative Heat Transfer Enhancement in Tubular Heat Exchanger: An Experimental Investigation with Minijet Impingement 管式热交换器中的创新传热增强技术:利用微型射流冲击的实验研究
Q3 Chemical Engineering Pub Date : 2024-05-04 DOI: 10.37934/arfmts.116.2.5158
Shital Yashwant Waware, Sandeep Sadashiv, A. Kurhade, Suhas Prakashrao Patil
This paper investigates heat transfer in a horizontally oriented tubular heat exchanger through a comprehensive examination of both numerical simulations and experimental analyses. The primary focus is on copper as the material of interest, specifically examining an inner tube with a 14 mm internal diameter and 1 mm thickness, as well as an outer tube with a 29 mm external diameter and 1 mm thickness. In addition to these components, two perforated pipes with internal diameters of 11 mm and 20 mm are incorporated; contributing to an overall length of the heat exchanger measuring 281 mm. Notably, the perforation pipe features a 5 mm diameter hole on its periphery. A comprehensive assessment was conducted to appraise heat transfer and coefficients within a straightforward tubular heat exchanger. The mass flow rate of chilled water in the annular space fluctuated between 0.01 kg/sec and 0.11 kg/sec, while the steady flow rate of hot water within the inner tube remained constant at 0.11 kg/sec. Inlet temperatures for the hot water were established at 55 °C, 75 °C, and 85 °C, with the cold water maintaining a consistent inlet temperature of 29 °C throughout the experiment.
本文通过对数值模拟和实验分析的综合研究,探讨了水平方向管式热交换器的传热问题。主要研究对象是铜材料,特别是研究内径为 14 毫米、厚度为 1 毫米的内管,以及外径为 29 毫米、厚度为 1 毫米的外管。除这些组件外,还包括两根内径分别为 11 毫米和 20 毫米的穿孔管,使热交换器的总长度达到 281 毫米。值得注意的是,穿孔管的外围有一个直径为 5 毫米的孔。为了评估直管式热交换器的传热和系数,我们进行了一项综合评估。环形空间中冷水的质量流量在 0.01 千克/秒和 0.11 千克/秒之间波动,而内管中热水的稳定流速则保持在 0.11 千克/秒。热水的入口温度分别为 55 °C、75 °C 和 85 °C,冷水的入口温度在整个实验过程中始终保持在 29 °C。
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引用次数: 0
Performance Analysis of a Crossflow Vortex Turbine for a Gravitational Water Vortex Power Plant 用于重力水涡流发电厂的横流涡轮性能分析
Q3 Chemical Engineering Pub Date : 2024-05-04 DOI: 10.37934/arfmts.116.2.1326
Abel Alfeuz, Fadzlita Tamiri, Farm Yan Yan, Wan Khairul Muzammil, Melvin Gan Jet Hong, Dayang Salyani Abang Mahmod, Nuramalina Bohari, Mohd Azlan Ismail
The micro hydro system is the most favorable renewable energy source to supply electricity for rural areas. The Gravitational Water Vortex Power Plant (GWVPP) is one of the micro hydro systems that is suitable for very low-head hydropower sites. GWVPP consists of three major parts: electromechanical components, civil structures, and electric distribution. The micro hydro turbine in GWVPP is called a vortex hydro turbine and is used to convert induced vortex flow to mechanical energy coupled with a generator to produce electricity. This paper investigates crossflow vortex turbine performance using Computational Fluid Dynamics (CFD) software and experimental work. The CFD results provide qualitative and quantitative comprising velocity distribution, water vortex profile, and water vortex height. The optimum hydraulic performance in the water vortex was observed and determined for different turbine positions. The vortex crossflow turbine was placed 0.05 m from the bottom surface of the basin at the highest vortex tangential velocity. A 0.05 m turbine position was chosen for the turbine installations as it creates a high-velocity profile. The comparative performance was conducted on the vortex crossflow blade with different inlet blade angle designs at a range of 400 – 700. The experimental analysis was conducted at rotational speeds of 30 rpm – 70 rpm to determine its efficiency performance. The optimum design for the crossflow blade was at 500 with an operational speed of 50 rpm, which exhibited torque and power output at 0.27±0.02 m and 1.49±0.08 m respectively with an efficiency recorded at 18.98%.
微型水力发电系统是为农村地区供电的最有利的可再生能源。重力水涡流发电站(GWVPP)是微型水力发电系统中的一种,适用于水头很低的水电站。GWVPP 由三大部分组成:机电部件、土建结构和配电装置。GWVPP 中的微型水轮机称为涡流水轮机,用于将诱导涡流转化为机械能,并与发电机耦合发电。本文利用计算流体动力学(CFD)软件和实验工作研究了横流涡轮机的性能。CFD 结果提供了定性和定量的速度分布、水漩涡剖面和水漩涡高度。观察并确定了不同涡轮位置下水涡的最佳水力性能。涡旋横流水轮机放置在距水池底面 0.05 米处,涡旋切向速度最大。选择 0.05 米的涡轮位置安装涡轮是因为它能产生高速剖面。在 400 - 700 的范围内,对具有不同入口叶片角度设计的涡旋横流叶片进行了性能比较。实验分析在 30 rpm - 70 rpm 的转速下进行,以确定其效率性能。横流叶片的最佳设计为 500,运行速度为 50 rpm,其扭矩和功率输出分别为 0.27±0.02 m 和 1.49±0.08 m,效率为 18.98%。
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引用次数: 0
Safe Energy using Hydraulic System Analysis at a Hydropower Plant 利用水电站水力系统分析实现安全能源
Q3 Chemical Engineering Pub Date : 2024-05-04 DOI: 10.37934/arfmts.116.2.131143
Wadhah Hussein Abdulrazzaq Al Doori, Ali Mohammed Hussien
The Hydro-PowerStation is one of the keys (important) sources of electricity, and it has a digital governor, which improves production efficiency over mechanical governors. This research looked at the hydraulic turbine, found flaws such as oil leakage from the pumps utilized, calculated the amount of energy consumed, and worked to reduce it by measuring the losses and monitoring the poor process during periods of high water load of up to 83%. As a consequence of the research, it was discovered that the amount of energy consumed had decreased by 20%, by employing well-made, effective pumps for each unit according to its use, oil leakage in all units is reduced.
水电站是电力的关键(重要)来源之一,它采用了数字调速器,与机械调速器相比提高了生产效率。这项研究考察了水轮机,发现了所使用水泵的漏油等缺陷,计算了能耗量,并通过测量损耗和监控高负荷(高达 83%)时的不良流程,努力降低能耗。研究结果表明,通过根据每个机组的使用情况为其配备制造精良、高效的水泵,减少了所有机组的漏油量,从而使能耗降低了 20%。
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引用次数: 0
The Effect of Insulation Thickness on Heat Transfer Characteristics and Flammability in Tube Mesoscale Combustors 隔热层厚度对管式中尺度燃烧器传热特性和可燃性的影响
Q3 Chemical Engineering Pub Date : 2024-05-04 DOI: 10.37934/arfmts.116.2.157171
Evita Leninda Fahriza Ayuni, Andinusa Rahmandhika, Daryono, Ardi Lesmawanto, Krisna Bayu Rizkyawan, Ali Mokhtar, Achmad Fauzan Hery Soegiharto
Micropower generator is a micro-scale energy source that has two main components, namely a micro/mesoscale combustor and thermophotovoltaics (TPV). The micro-scale combustor is one part that functions as a combustion chamber that produces heat in micropower plants. Heptane is used as fuel, while the combustor combustion chamber with a diameter of 3.5 mm is made from duraluminium-quart glass tube. Combustion stability in the combustion chamber is influenced by several factors, such as temperature, geometry, and combustion chamber design. In order to maintain flame stability, mesh is added to the combustion chamber. One way to minimize heat loss in the combustion chamber is to add an insulating layer to the combustion chamber. This research aims to prove the role of adding an insulating layer in flame stability in mesoscale burners. It is necessary to add an appropriate insulating layer to minimize heat loss so that it remains stable in the mesoscale burner. This experimental test shows that the temperature distribution when adding an insulation layer with a thickness of 3 mm has a higher temperature on the outside compared to a thickness of 6 mm. Meanwhile, the temperature inside the combustor chamber with a thickness of 6 mm is superior to that with a thickness of 3 mm. The flame limit of the combustor with a mesh distance of 5 mm for liquid heptane fuel was successfully stable at an equivalent ratio of ɸ0.97 – 1.5 with a maximum speed of 31.7.
微型发电设备是一种微型能源,由两个主要部分组成,即微型/中型燃烧器和热光电(TPV)。微尺度燃烧器是微型发电站中作为燃烧室产生热量的一部分。庚烷被用作燃料,而直径为 3.5 毫米的燃烧器燃烧室则由杜拉铝夸脱玻璃管制成。燃烧室中的燃烧稳定性受多种因素影响,如温度、几何形状和燃烧室设计。为了保持火焰的稳定性,需要在燃烧室中添加网格。尽量减少燃烧室热量损失的一种方法是在燃烧室中添加隔热层。本研究旨在证明在中尺度燃烧器中添加隔热层对火焰稳定性的作用。有必要添加适当的隔热层,以尽量减少热量损失,从而在中尺度燃烧器中保持稳定。该实验测试表明,与厚度为 6 毫米的隔热层相比,添加厚度为 3 毫米的隔热层时,外部的温度分布较高。同时,厚度为 6 毫米的燃烧室内部温度要高于厚度为 3 毫米的燃烧室。对于液态庚烷燃料,网距为 5 毫米的燃烧器的火焰极限成功稳定在当量比 ɸ0.97 - 1.5 和最大速度 31.7 之间。
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引用次数: 0
Extended Eddy-Viscosity Model to Rayleigh-Benard Convection in Cavity 腔体内瑞利-贝纳德对流的扩展涡粘模型
Q3 Chemical Engineering Pub Date : 2024-05-04 DOI: 10.37934/arfmts.116.2.102111
Gunarjo Suryanto Budi, Sasa Kenjeres
This paper presents a study of developing a numerical turbulent model in a cavity heated from below using eddy viscosity combined with elliptic relaxation approach. The model uses a set of differential equations that consist of kinetic energy, its dissipation, variance of temperature, velocity scale and elliptic relaxation parameter, which are solved using a finite-volume and Navier-Stokes solver. The unresolved stress tensors and heat flux vectors are modelled with an algebraic formula. The discretization method is carried out by CDS, or second-order differencing scheme, and LUDS, or second-order linear upwind scheme. The model is applied to the natural convection heated from below, known as Rayleigh-Benard convection, in a two-dimensional cavity with a height-to-length aspect ratio of 1:1.5, 1:4, and 1:8. The model has been validated using numerical data from DNS (direct numerical simulation) and experiments. The model produced similar results with both DNS and experiments. It was also shown that the model can visualize the main feature of turbulent convective flow in the enclosure for various aspect ratio.
本文介绍了利用涡粘与椭圆松弛相结合的方法在一个从下往上加热的空腔中建立湍流数值模型的研究。该模型使用一组微分方程,包括动能、动能耗散、温度变化、速度尺度和椭圆松弛参数,并使用有限体积和纳维-斯托克斯求解器求解。未解决的应力张量和热通量向量用代数公式建模。离散化方法采用 CDS(二阶差分方案)和 LUDS(二阶线性上风方案)。该模型适用于高度与长度长宽比分别为 1:1.5、1:4 和 1:8 的二维空腔中自下而上受热的自然对流(即瑞利-贝纳德对流)。该模型利用 DNS(直接数值模拟)和实验的数值数据进行了验证。该模型与 DNS 和实验结果相似。实验还表明,该模型可以直观地显示不同长宽比的围护结构中湍流对流的主要特征。
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引用次数: 0
Stretched Meshing in a 2D Computational Domain with Elbow Edges for CFD Applications 二维计算域中的拉伸网格与 CFD 应用中的肘部边缘
Q3 Chemical Engineering Pub Date : 2024-05-04 DOI: 10.37934/arfmts.116.2.4150
Gancang Saroja, Sugeng Rianto, Abdurrouf, S. P. Sakti, M. Nurhuda
Mesh generation is critical for obtaining accurate and detailed solutions to mesh-based numerical problems, particularly when capturing specific information within a designated area of the domain. While structured meshes offer consistency, their uniform resolution limits their ability to achieve this. Mesh stretching offers a solution by introducing non-uniform element sizes based on an analytical relationship while preserving the original mesh structure. The objective of this study is to create a hybrid mesh model that leverages the strengths of both structured and stretched meshes. A 2D rectangle with elbow edges serves as the domain. To address the requirements of CFD applications, the domain is refined by increasing element density near the boundaries and corners. Skewness, aspect ratio, and element quality are then assessed to determine the overall mesh quality. The results demonstrate that stretching the structured mesh produced a mesh with quality that meets CFD domain standards.
网格生成对于获得基于网格的数值问题的精确而详细的解决方案至关重要,尤其是在捕捉域中指定区域内的特定信息时。虽然结构网格具有一致性,但其统一的分辨率限制了其实现一致性的能力。网格拉伸提供了一种解决方案,即在保留原始网格结构的同时,根据分析关系引入非均匀元素尺寸。本研究的目的是创建一个混合网格模型,充分利用结构网格和拉伸网格的优势。以带有肘形边缘的二维矩形为域。为了满足 CFD 应用的要求,通过增加边界和边角附近的元素密度来细化该域。然后对斜度、长宽比和元素质量进行评估,以确定整体网格质量。结果表明,拉伸结构化网格所产生的网格质量符合 CFD 域标准。
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引用次数: 0
Simulation of the Effect of Air Humidity Ratio in the Drying Room on the Rate of Material Evaporation in Vacuum Freeze Drying 模拟干燥室空气湿度比对真空冷冻干燥中材料蒸发速率的影响
Q3 Chemical Engineering Pub Date : 2024-05-04 DOI: 10.37934/arfmts.116.2.144156
I. Buana, E. Kosasih
In the drying process there are several parameters that influence the evaporation rate. Apart from pressure and temperature, air humidity in the drying room has been shown to influence the evaporation rate. To find out how much influence air humidity has on the evaporation rate in a Vacuum Freeze Dryer (VFD) system, calculations and simulations need to be carried out. Evaporation in a VFD occurs by sublimation at evaporation conditions below the triple point of water. Ice weighing 2x10-2 kg was used as dry material to characterize the VFD process at a temperature of -10oC. The ice temperature and operating pressure are selected at conditions below the triple point so that sublimation evaporation occurs. The temperature of the drying room for heating was varied, namely (20, 25, 30)(oC) and pressure (0.5, 0.4, 0.3)(kPa). Air humidity ratio, varies at (300, 200, 100, 10, 1, 0.1, 0.01, 0.001) (kg H2O/kg dry air). The simulation is carried out in a drying room, the ice receives heat due to the temperature difference with room temperature, heat transfer occurs by radiation and diffusion. Heat is used to evaporate the ice through sublimation. The temperature of the ice upon sublimation is close to the wet bulb temperature and remains constant until the ice has completely evaporated. From the simulation it is known that changing the air humidity ratio in the drying room from 300 (kg H2O/kg dry air) to 0.001 (kg H2O/kg dry air) will increase the evaporation rate between 6.2% - 9.5%. The evaporation rate increased by 6.2% was obtained at P∞=0.3kPa, T∞=30oC. This increase in evaporation rate shortened the drying time by 0.42 hours. The evaporation rate increased by 9.5% at a pressure of P∞=0.5kPA, T∞=20oC thereby shortening the drying time by 1.03 hours. Simulations show that increasing the evaporation rate and shortening the drying time has the potential to increase the energy efficiency of the VFD. The increase in evaporation rate is influenced by operating temperature and pressure. Simulations confirmed that the evaporation rate increased when the drying chamber temperature was increased and the air pressure was decreased.
在干燥过程中,有几个参数会影响蒸发率。除压力和温度外,干燥室的空气湿度也会影响蒸发率。为了解空气湿度对真空冷冻干燥机(VFD)系统中蒸发率的影响程度,需要进行计算和模拟。真空冷冻干燥机中的蒸发是在低于水的三相点的蒸发条件下通过升华进行的。重量为 2x10-2 千克的冰被用作干燥材料,以表征温度为 -10oC 的 VFD 过程。冰的温度和工作压力都选在低于三相点的条件下,以便发生升华蒸发。加热干燥室的温度变化为(20、25、30)(oC),压力变化为(0.5、0.4、0.3)(kPa)。空气湿度比在 (300, 200, 100, 10, 1, 0.1, 0.01, 0.001) (kg H2O/kg dry air) 下变化。模拟在烘干室中进行,冰块因与室温的温差而受热,热量通过辐射和扩散传递。热量用于通过升华蒸发冰。升华后冰的温度接近湿球温度,并保持恒定,直到冰完全蒸发。通过模拟可知,将烘干室的空气湿度比从 300(千克水/千克干空气)改为 0.001(千克水/千克干空气)将使蒸发率提高 6.2% - 9.5%。在 P∞=0.3kPa、T∞=30oC 时,蒸发率增加了 6.2%。蒸发率的增加使干燥时间缩短了 0.42 小时。当压力 P∞=0.5kPA, T∞=20oC 时,蒸发率增加了 9.5%,从而使干燥时间缩短了 1.03 小时。模拟结果表明,提高蒸发率和缩短干燥时间有可能提高变频驱动装置的能效。蒸发率的提高受工作温度和压力的影响。模拟证实,当干燥室温度升高、气压降低时,蒸发率会增加。
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引用次数: 0
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Journal of Advanced Research in Fluid Mechanics and Thermal Sciences
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