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Chapter 1 Solute Transport In Biological Systems Example 1.3-1. ---------------------------------------------------------------------------------An experimental reverse osmosis membrane is being used to produce a waste stream that is Na2CO3 solution. The pure water flux at 30oC is measured as Jsolvent = 1500 L/m2day when p = 25 atm. With the Na2CO3 solution (5 wt% Na2CO3) operation is at 30oC with PH = 50 atm and PL = 1 atm. Both permeate and feed sides of the membrane are perfectly mixed. Find Jsolvent for the 5 wt% Na2CO3 solution. The vapor pressure of water over 5 wt% Na2CO3 solution is 31.2 mmHg. Solution ------------------------------------------------------------------------------------------ Membrane 1 atm 50 atm Pfeed-Ppermeate Water 5 wt% Na2CO3 feed-permeate) Low pressure (permeate) side High pressure (feed) side Figure 1.3-5 Flow of water by reverse osmosis. The solvent volumetric flow rate is given by Jsolvent = LpS[(Pfeed Ppermeate) (feed permeate)] We can determine the product LpS from pure water flow data when (feed permeate) = 0 LpS = J solvent 1500 = = 60 L/m2dayatm 25 Pfeed Ppermeate When the feed side is 5 wt% Na2CO3 solution, the osmotic pressure must be determined. We will consider two cases: ideal and non-ideal solution. 1-11 1) For ideal solution, the osmotic pressure on the feed side is given by = RT CS Density of Na2CO3 is 2.533 g/cm3, and density of water is 1 g/cm3. For 1000 g of 5 wt% Na2CO3 solution we have 950 g of water and 50 g of Na2CO3. Since the molecular weight of Na2CO3 is 106, CS is computed as CS = 50 / 106 = 4.8610-4 mol/cm3 950 / 1 50 / 2.533 With the ideal gas constant R = 82.057 cm3atm/moloK, the osmotic pressure for the feed side is = (82.057)(30 + 273.15)(4.8610-4) = 12.1 atm The solvent flow rate is then determined Jsolvent = LpS[(Pfeed Ppermeate) (feed permeate)] Pfeed Ppermeate = 50 1 = 49 atm feed permeate = 12.1 0 = 12.1 atm Jsolvent = 60[49 12.1] = 2814 L/m2day 2) For non-ideal solution, the osmotic pressure on the feed side is given by = RT ln W xW L VW The activity coefficient W in 5 wt% Na2CO3 solution can be obtained from the requirement that the fugacity of water in the solution is the same as the fugacity of water vapor in equilibrium with the solution f WL = f WV xW W PWo = yWP = PW xW W = PW PWo At 30oC, vapor pressure of water is PWo = 31.824 mmHg, vapor pressure of 5 wt% Na2CO3 L solution is PW = 31.2 mmHg, and V W = 18.095 cm3/mol. Therefore = P (82.057)( 303.15) 31.2 RT ln Wo = ln = 27.2 atm L 18.095 31.824 PW VW The solvent flow rate is then 1-12 Jsolvent = LpS[(Pfeed Ppermeate) (feed permeate)] Jsolvent = 60[49 – 27.2] = 1307 L/m2day The assumption of ideal solution can produce a significant error. --------------------------------------------------------------------------------------------------Table 1.2-1 lists the osmotic pressure of aqueous sucrose solution at 30oC calculated using equation (1.2-3) for non-ideal solution and equation (1.2-5) for ideal solution. The values for non-ideal model agree well with the experimental data. RT ln WA xWA L VW (1.2-3) RT A x S = RT CS L VW (1.2-5) = = Table 1.2-1 Osmotic pressure (atm) of aqueous sucrose solution at 30oC CS (mol/liter) Eq. (1.2-5) Eq. (1.2-3) Exp. Data 0.991 20.3 26.8 27.2 1.646 30.3 47.3 47.5 2.366 39.0 72.6 72.5 3.263 47.8 107.6 105.9 4.108 54.2 143.3 144.0 5.332 61.5 199.0 204.3 1.4 Regulation of Extracellular Fluid Osmolality1 Water that is consumed is absorbed from the intestines and enters the extracellular fluid. An increase in the osmolality of the extracellular fluid triggers thirst and antidiuretic hormone (ADH) secretion. ADH acts on the distal tubules and collecting ducts of the kidneys to increase reabsorption of water from the filtrate. The increase in the amount of water entering the extracellular fluid causes a decrease in osmolality. A decrease in extracellular fluid osmolality inhibits thirst and ADH secretion. Less water is consumed, and less water is reabsorbed from the filtrate in the kidney. Consequently, more water is lost as a large volume of dilute urine. The result is an increase in the osmolality of the extracellular fluid. The ADH and thirst mechanism are sensitive to even small changes in extracellular fluid osmolality and the response in fast (from minutes to a few hours). The hormonal regulation of blood osmolality is illustrated in Figure 1.4-1. The diencephalon, part of the brain between the brainstem and the cerebrum, is shown in Figure 1.4-2. Its main components are the thalamus, subthalamus, epithalamus, and hypothalamus. 1 Seeley R.R, Stephens T.D., Tate P., Anatomy & Physiology, McGraw Hill, 2003, p. 989 1-13 Blood osmolality (normal range) An increase in blood osmolality is detected by osmoreceptors in the hypothalamus An decrease in blood osmolality is detected by osmoreceptors in the hypothalamus Osmoreceptors stimulate ADH secretion from the posterior pituitary and increase thirst Osmoreceptors inhibit ADH secretion from the posterior pituitary and decrease thirst * Increased ADH increases the permeability of the distal tubules and collecting ducts to water. More water returns to the blood and less water is lost in the urine. * Decreased ADH decreases the permeability of the distal tubules and collecting ducts to water. Less water returns to the blood and more water is lost in the urine. * Increased thirst increases water intake, resulting in the increased movement of water into the blood * Decreased thirst decreases water intake, resulting in the decreased movement of water into the blood. A decrease in blood osmolality results from the increased movement of water into the blood An increase in blood osmolality results from the decreased movement of water into the blood Blood osmolality (normal range) Figure 1.4-1 Hormonal regulation of blood osmolality. Figure 1.4-2 A graphical depiction of the diencephalon. 1-14