Forward osmosis concentration of a vanadium leaching solution

Uranium concentration from acidic mine effluent using forward osmosis

Uranium (U) is found in the earth's crust at concentrations ca. 1 to 3 ppm, which presents opportunities for various industrial and hydrometallurgical processes aimed at achieving economical and low-energy-intensive extraction. In this study, we assessed the potential of forward osmosis (FO) to concentrate the uranium mine effluent using sodium sulphate as draw solution. The diluted draw solution can be directly reused as a raw material in the uranium leaching process without the need for regeneration. Laboratory FO experiments were performed for 160 h duration on synthetic uranium solution representing typical mine effluent characteristics of the Jadguda uranium extraction facility, Bihar, India. The results of the study showed that with forward osmosis, uranium can be concentrated to ca. 3.36 times of its initial concentration and ca. 98% rejection, but with considerable flux decline due to membrane fouling and surface crystallization. Further, the membrane can be operated after regeneration using DI water rinsing or physical cleaning with a lower flux recovery of 83.1% and 81.2%, respectively. Importantly, it was observed that operating membrane below critical concentration factor via cyclic mode can avoid surface crystallization and subsequent membrane fouling with least periodic maintenance. Additionally, with FO concentration process the U concentration much lesser than Indian regulatory guidelines for inland water discharge (i.e. 180μg of U L-1) could be achieved using draw solution. Our study highlights that the FO concentration process can significantly concentrate uranium mine effluent at room temperature, requiring less specific energy compared to conventional evaporation-based processes that are highly energy-intensive.

Phallusia nigra-mediated vanadium removal from brine: Assessment and optimization

The rejected brines from desalination plants contain significant amounts of heavy metals. In this study, we evaluated the effectiveness of Phallusia nigra Savigny, 1816 (P. nigra) in removing vanadium from the rejected brines of desalination plants through the bioaccumulation process. Initial assessments revealed a remarkably high accumulation rate of vanadium in P. nigra with a bioaccumulation factor exceeding 4.7 × 104 in the tunic and 5.1 × 105 in the mantle body. Acclimation experiments demonstrated that P. nigra could survive salinities up to 56 practical salinity units (psu), temperatures of ≤32 °C, and pH of 6.5-8.5. We employed the L-16 Taguchi approach in experimental design to optimize environmental conditions for vanadium removal by P.nigra. Our results indicated that temperature has the most significant effect on increasing vanadium bioaccumulation in P. nigra, followed by salinity and pH. Under optimal conditions, the vanadium concentration reached 1892.30 ppm in the entire body of P. nigra compared to 350 ppm in natural conditions. Considering that, a high concentration of vanadium is toxic to the environment and the conventional methods of its removal from brine are costly and include the use of chemicals that pollute the environment, therefore, vanadium removal from brine using P. nigra can be considered a cost-effective and environmentally friendly method in the future, as opposed to some chemical methods.

Forward Osmosis for Metal Processing Effluents under Similar Osmotic Pressure Gradients

Water recovery from aqueous effluents in the mining and metals processing industry poses a unique challenge due to the high concentration of dissolved salts typically requiring energy intensive methods of treatment. Forward osmosis (FO) is a lower energy technology which employs a draw solution to osmotically extract water through a semi-permeable membrane further concentrating any feed. Successful FO operation relies on using a draw solution of higher osmotic pressure than the feed to extract water while minimizing concentration polarization to maximize the water flux. Previous studies employing FO on industrial feed samples commonly used concentration instead of osmotic pressures for feed and draw characterization; this led to misleading conclusions on the impact of design variables on water flux performance. By employing a factorial design of experiments methodology, this study examined the independent and interactive effects on water flux by: osmotic pressure gradient, crossflow velocity, draw salt type, and membrane orientation. With a commercial FO membrane, this work tested a solvent extraction raffinate and a mine water effluent sample to demonstrate application significance. By optimizing with osmotic gradient independent variables, water flux can be improved by over 30% without increasing energy costs or compromising the 95-99% salt rejection of the membrane.

Feasibility of osmotic dilution for recycling spent dialysate: Process performance, scaling, and economic evaluation

Hemodialysis is one of the therapies for patients with kidney failure. Hemodialysis requires large amounts of pure water, and is one of the most water-hungry medical procedures, and thus represents a clear opportunity where improvements should be made concerning the consumption and wastage of water. In this paper, we explored the potential of forward osmosis (FO) membrane for recycling the spent dialysate using the dialysis concentrate as the draw solution. Partially diluted dialysis concentrate could be further diluted with pure water to form dialysate for further dialysis process. Using commercial cellulose triacetate (CTA) FO membranes, the water recovery of approximately 64% was achieved and the final volume of the partially diluted dialysis concentrate was about four times the initial volume. Flux decline of the FO process was observed, mainly due to concentration of synthetic spent dialysate and dilution of dialysis concentrate, while membrane scaling had little impact on the flux decline. The urea rejection was found to be relatively low owing to the small size and electroneutral nature of the urea molecule. Obvious membrane scaling was observed after three FO cycles. The energy dispersive spectroscopy analysis of the scaling layer indicated that the scalants were phosphates and carbonates. The scaling was removed via osmotic backwash and almost completely recovery of FO flux was obtained. Economic analysis showed that the centralized treatment of spent dialysate in a dialysis center using the proposed osmotic dilution process could greatly save water resources and cost. Improving the urea rejection of FO membrane was identified as an important research focus for future research on the potential application of FO technology for recycling the spent dialysate in hemodialysis.

Modelling Forward Osmosis Treatment of Automobile Wastewaters

Forward osmosis (FO) has rarely been investigated as a treatment technology for industrial wastewaters. Within this study, common FO model equations were applied to simulate forward osmosis treatment of industrial wastewaters from the automobile industry. Three different models from literature were used and compared. Permeate and reverse solute flux modelling was implemented using MS Excel with a Generalized Reduced Gradient (GRG) Nonlinear Solver. For the industrial effluents, the unknown diffusion coefficients were calibrated and the influences of the membrane parameters were investigated. Experimental data was used to evaluate the models. It could be proven that common model equations can describe FO treatment of industrial effluents from the automobile industry. Even with few known solution properties, it was possible to determine permeate fluxes and draw conclusions about mass transport. However, the membrane parameters, which are apparently not solution independent and seem to differ for each industrial effluent, are critical values. Fouling was not included in the model equations although it is a crucial point in FO treatment of industrial wastewaters. But precisely for this reason, modelling is a good complement to laboratory experiments since the difference between the results allows conclusions to be drawn about fouling.