Mathematical Analysis of Sub-Atmospheric Vapor Pipeline (SAVP) Transmission for Seawater Desalination

M. Shojaei, M. Nosrati, R. Attarnejad
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Abstract

Seawater desalination by sub-atmospheric vapor pipeline transfer (known as SAVP) is one of the innovative seawater desalination methods that could be used in lands and industries. SAVP systems works based on the temperature difference between a hot source and a cold environment; this method can provide users with a variety of advantages in industrial and field applications. The temperature of the hot and cold sources, as boundary conditions, can be considered as a function of time in natural and industrial environments; therefore, it affects the process of convection and diffusion significantly. In such a case, new and interesting challenges arise; such as reviewing and simplifying the basic convection-diffusion equation through obtaining the temperature profile in the pipeline by using advanced engineering mathematics. Two mathematical approaches can be developed to solve the temperature differential equation; one is through Eigen functions and the other one uses Green’s equation based on the length of the pipeline for SAVP. In this study, vapor’s temperature will be formulated as a function of time and length in accordance with the given assumptions and information. Mathematical simulations were performed for a field-scale spanning between Bandar Abbas and Geno (two places on the south coast of Iran) biosphere reserve. Also, an industrial scale in a vapor transfer device with a heat source capacity of about 200 liters was assembled. The results showed an acceptable range of accuracy in the proposed methods.
海水淡化低压蒸汽管道(SAVP)输送的数学分析
亚大气蒸汽管道输送海水淡化技术(SAVP)是一种创新的海水淡化方法,可用于土地和工业。SAVP系统的工作原理是基于热源和冷环境之间的温差;这种方法可以为用户在工业和现场应用中提供多种优势。在自然环境和工业环境中,冷热源的温度作为边界条件可以看作是时间的函数;因此,它对对流和扩散过程的影响很大。在这种情况下,新的和有趣的挑战出现了;如利用高等工程数学的方法,对管道内温度分布的基本对流扩散方程进行了回顾和简化。可以采用两种数学方法来求解温度微分方程;一种是通过特征函数,另一种是基于管道长度的格林方程。在本研究中,根据给定的假设和信息,蒸汽的温度将被表示为时间和长度的函数。对阿巴斯港和吉诺(伊朗南部海岸的两个地方)生物圈保护区进行了野外尺度的数学模拟。此外,还组装了一个工业规模的蒸汽传递装置,其热源容量约为200升。结果表明,所提出的方法在可接受的精度范围内。
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