Reverse Osmosis Industry: Product: Refining, Food and beverage, Power, Oil and Gas, Pulp and Paper, Chemical, Water pH/ORP Meters Background Information Reverse osmosis (RO) is a separation process that uses pressure to force a solution through a membrane that retains the solute on one side and allows the pure solvent to pass to the other side. More formally, it is the process of forcing a solvent from a region of high solute concentration through a membrane to a region of low solute concentration by applying a pressure in excess of the osmotic pressure. To illustrate, imagine a semipermeable membrane with fresh water on one side and a concentrated aqueous solution on the other side. If normal osmosis takes place, the fresh water will cross the membrane to dilute the concentrated solution. In reverse osmosis, pressure is exerted on the side with the concentrated solution to force the water molecules across the membrane to the fresh water side. which the pure water flows through the membrane is determined by water temperature and factors listed above. By design, not all feedwater passes through the membrane. Some feedwater is piped to flow over the membrane. This diverted feedwater cleans away the rejected impurities in a cross-flow filtration mode. An RO machine, produces one purified water stream called permeate and a second stream called concentrate, brine, or reject from one feedwater stream. Feedwater enters the machine is fairly low pressure. Water flows through pre-filters to remove suspended particles, such as silt. These replaceable pre-filters provide a cost effective method to keep the membrane clean. Since RO necessitates the use of pressure, normally this pressure is provided by a water pump that overcomes energy differences (osmotic pressure) that drives feedwater through a porous, semipermeable membrane. This semipermeable membrane permits pure water to pass through, but inhibits the majority of dissolved impurities, from passing through. The impurities fail to pass through the membrane for two reasons: I.) They are blocked due to physical size (organics and biologicals) II.) They are blocked as a result of electrical charge repulsion (inorganic salts). RO membranes (Polyamide thin-film composites) are designed to have very small pores or holes. These holes permit the passage of water. A slight amount of impurities the feedwater will be carried through into the purified water. The amount of impurities found in the purified water depends on such things as the type of membrane, condition of the membrane (i.e. age, cleanliness) and the amount of pressure applied (energy). The percent concentration of impurities is normally less than 5% of feedwater content. The rate at AN10B01B20-06E http://www.yokogawa.com RO systems are intended to run automatically. They require only periodic operating data collection and routine maintenance. Most modern systems are equipped with performance monitoring equipment to call for operator assistance or in more extreme situations, to automatically shut down the RO system. RO systems also have instrumentation to measure process conditions. These include permeate flow rate and conductivity, machine feed and discharge pressure feed pH, and the calculable percentage recovery. All measurements represent machine operating characteristics and are based on the machine’s design. Consistency in each of the values indicates the machine is operating properly. Given the fact that RO systems use up consumable products during operation, cartridge pre-filters are typically replaced every two weeks. Separator (membrane elements) life, however, is approximately three years. All other components of a machine are considered “hardware” and should not require replacement other than through normal mechanical wear and tear. RO performance is optimized under a regular maintenance program. Activities within the program include adding grease or oil to the high-pressure pump, changing pre-filters, sanitizing the machine, and cleaning the separators when they become fouled. Pretreatment equipment, such as softeners, and instruments such as pH analyzers requires attention as well. General Applications Reverse Osmosis, also known as hyper-filtration, is the finest filtration known. This process will allow the removal of particles as small as ions from a solution. RO systems frequently are used to reduce the levels of total dissolved solids and suspended particles within water. These systems remove a variety of ions and metals as well as certain organic, inorganic and bacterial contaminants. Reverse osmosis is used to purify water and remove salts and other impurities in order to improve the color, taste or properties of the fluid. Reverse osmosis is often used in commercial and residential water filtration. It is also one of the methods used to desalinate seawater. Sometimes reverse osmosis is used to purify liquids in which water is an undesirable impurity (e.g., ethanol). The RO membrane alone may not be an effective method for total removal of these contaminants, but properly designed system may be effective in reducing the contaminants to safe levels. The RO membrane’s efficiency in reducing the amount of contaminant in the water depends on the contaminant concentration, chemical properties of the contaminant, the membrane type and condition, and opening conditions. The most common use for RO is in purifying water. It is used to remove dissolved impurities from water through the use of separation technology and a semi-permeable membrane, to meet the most demanding specifications that are currently in place. Reverse osmosis is capable of rejecting bacteria, salts, sugars, proteins, particles, dyes, and other constituents that have a molecular weight of greater than 150-250 Daltons. The separation of ions with reverse osmosis is aided by charged particles. This means that dissolved ions that carry a charge, such as salts, are more likely to be rejected by the membrane than those that are not charged, such as organics. The larger the charge and the larger the particle, the more likely it will be rejected. All Rights Reserved, Copyright © 2014, Yokogawa Corporation of America Pure Water Applications Membrane rejection fluctuates regarding the following factors: I.) Total Dissolved Solids (TDS) II.) pH Values III.) Cross flow rates and IV.) Element recovery levels The performance of elements (membrane) in the secondpass of a reverse osmosis (RO) system can be the most dramatically affected. These variations, while not significant in the majority of applications, become crucial to the success of high-purity water processing. In addition, the effect of minor feedwater constituents, such as alkalinity and ammonia, as seen to play a dominant role in achieving highpurity permeate. The reverse osmosis (RO) membrane of choice worldwide is the polyamide (PA) thinfilm composite membrane developed by Cadotte (1980). The PA composite membrane is made by forming a thin PA film on the finely porous surface of a polysulfone (PS) supporting membrane by an interfacial reaction between the reactant pair trimesoyl chloride (TMC) and m-phenylenediamine (MPD). PA membranes have a surface charge that plays a role in their separation capability. It is important to note that the nature of this charge can be altered by the pH of the feedwater pH. The majority of PA (RO) membranes are negatively charged when operated on pH levels most commonly encountered in water applications. RO systems performance is pH sensitive. The pH at which a protein, RO membrane, carries no net charge is called the membranes isoelectric point. Below the isoelectric point, which is normally between pH 4 and 5, the proteins carry a net positive charge, above it a net negative charge. Due to a preponderance of weakly acid residues in almost all proteins, they are nearly all negatively charged at neutral pH. The isoelectric point is of significance in protein purification because it is the pH at which solubility is often minimal and at which mobility in an electrofocusing system is zero (and therefore the point at which the protein will accumulate). This substantially decreases their performance when the permeate quality is being measured by conductivity. Acid transport across the membrane explains much of this decrease in performance. Fortunately, this breakdown is completely reversible when the pH is returned to nearneutral levels. The acid transport is facilitated by the presence of un-reacted amines in the polyamide barrier layer. Any particular membrane can respond differently to changes in pH. High pH levels can also reduce the rejection capabilities of PA membranes as measured by conductivity. When values climb above a pH of 8.5, problems can occur. Lowering the pH via acid addition will correct this condition. Thin-film composite Polyamide membrane performance is also a function of the relative conductance of the feedwater. Below a certain level of TDS, the membrane rejection will decline with the TDS of the feed solution. This means it is possible to have a first-pass permeate that is “too pure” for the optimum overall performance of a two-pass RO system. Membrane separation efficiency is affected by feedwater chemistry. Chemistry takes the dominant role when the desired product is high-purity water and the benchmark is conductivity. Dissolved gases such as carbon dioxide (CO2) can dramatically affect permeate conductivity and RO systems cannot effectively deal with these gases by themselves. In specific case of CO2, it is possible to force a -2 conversion to bicarbonate (HCO3) and carbonate (CO3 ) ions by raising the feedwater pH. These ions are well rejected by PA (RO) membranes whereas CO2 (and carbonic acid) are not rejected at all. By controlling the pH of the feed solution, a portion of the CO2 present can be shifted to HCO3 and/or CO3-2 depending on the pH level reached. These pH adjustments permit up to 98% percent of bicarbonate and carbonate being removed in the first pass of a two-pass system. Sometimes it is not possible to elevate the pH of the feedwater. The same objective (removal of some of the feedwater alkalinity and CO2) can be reached by the use of degasifier. The degasifier can be located ahead of the first RO machine or between the two passes. Should some alkalinity pass into the RO permeate, it will re-equilibrate, forming H2CO3, HCO3 and/or CO3-2 in proportion to the pH. Ammonia is yet another water chemistry variable that plays a significant role in achieving high purity water. Ammonia may be present due to municipal chlorination of feedwater or from organic contamination. Residual ammonia may also be present in the water during the feedwater treatment by activated carbon or ion exchange via the subsequent liberation of ammonia. At neutral and acidic pH values ammonia is ionized. This means the addition of a strong alkali will produce molecular ammonia. Should the feedwater contain ammonia, the need to add caustic for CO2 removal must be carefully balanced with the need to eliminate ammonia in the permeate. Ammonia (NH3) can pass through the membrane system in 4+ either the molecular or ionic (NH ) form. Ammonium hydroxide (NH4OH) would be the most likely ionic form to pass through RO (thin-film composite Polyamide) All Rights Reserved, Copyright © 2014, Yokogawa Corporation of America membrane, particularly if caustic is being used to raise the pH in the system. Ammonium hydroxide is less conductive than ammonium carbonate [(NH4)2CO3] so it is not uncommon to find off-line samples or storage tank water with conductivity higher than that of on-line readings. The pH values will be lower. This shift in pH is due to absorption of CO2 from the air and the formation of carbonic acid in the water. Without the presence of ammonia, this type of contamination of high-purity water with CO2 would generate higher conductivity as well as the reduced pH. Product Recommendations Measurement System Transmitter/Analyzer • • 2-wire FLXA21 pH/ ORP measurement system 4-wire PH450G pH/ORP measurement system Option 1: Holders • • FF20 Flow-thru assembly with individual measure, reference and temperature electrodes FS20 Insertion assembly with individual measure, reference and temperature electrodes Sensors Bellowmatic reference electrode (SR20-AC32), coupled with the shock-proof measuring electrode (SM21-AG4) and Pt1000 temperature electrode (SM60-T1) Option 2: Holder: PH8HH Flow Thru assembly Sensor: PH8EHP Flowing reference pH Sensor for High Purity Water
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