Hollow fiber reverse osmosis: experiments and analysis of radial flow systems
โ Scribed by Muru S. Dandavati; Mahendra R. Doshi; William N. Gill
- Publisher
- Elsevier Science
- Year
- 1975
- Tongue
- English
- Weight
- 815 KB
- Volume
- 30
- Category
- Article
- ISSN
- 0009-2509
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โฆ Synopsis
The performance of a hollow fiber reverse osmosis system was determined experimentally by measuring the fraction of feed recovered as product, 4, and the concentration reduction ratio, 0,. A predictive model for these two quantities was developed which yields results that agree with the experimental data very well for applied pressures of 300450 psig., feed rates from 75 to 525 cclsec and feed concentrations up to 15000 ppm of sodium chloride.
The concept of distributed sinks in a continuum is used for the shell side, and a diffusion model is used to describe solute transport across the fiber wall. The principal assumptions made are negligible concentration polarization, small radial pressure drop in the shell and small solute transport, compared with solvent transport, through the fiber. Simple closed form expressions for Q and B,, given by eqns (43a) and ( 51) were obtained which are accurate over the range of experimental conditions employed. lNTBODIJCTiON Gill and Bansalll, 2,5], developed a detailed analysis and presented experimental data describing mass and momen-
๐ SIMILAR VOLUMES
A number of investigators have made efforts to develop various analytical models for hollow fiber type reverse osmosis (RO) module systems since the 1970s. However, a perfect analytical model, which c~m precisely explain the observed RO performances under a wide range of operating conditions has not
The presently used hollow fiber membrane modules consist of a bundle of fibers in a cylindrical polymer or metal shell parallel to the shell axis . The feed solution flows either through the lumen or at the outside parallel to the fibers . This paper compares the performance of these modules with a
The three parameter model of Kedem and Katchalsky [l] for describing the mass transport across a membrane is used for developing the design equations for reverse osmosis (RO) systems. It is shown that by using a simplifying assumption of replacing the local solute permeate concentrations by the aver
Analytical expressions describing convective flow in a continuous arteriovenous hollow fiber hemofilter were developed. In the lumen of the hollow fiber membrane, existing analytical expressions were applied to describe velocity profiles and pressure. For flow in the shell (the extracapillary space