Effect of Temperature

We have learned from previous chapters that equilibrium and reaction constants are affected by temperature. The length of time that a disinfection process proceeds is a function of the constants of the underlying reaction between the microorganism and the disinfectant thus, it must also be a function of temperature. The variation of the contact time to effect a given percentage kill with respect to temperature can therefore be modeled by means of the Van't Hoff equation. This equation was...

Info

Settling has been defined as a unit operation in which solids are drawn toward a source of attraction. The particular type of settling that will be discussed in this section is gravitational settling. It should be noted that settling is different from sedimentation, although some authors consider settling the same as sedimentation. Strictly speaking, sedimentation refers to the condition whereby the solids are already at the bottom and in the process of sedimenting. Settling is not yet...

Problems

12.1 A raw water containing 140 mg L of dissolved solids is subjected to coagulation treatment using alum. The optimum pH was determined to be equal to 5.32 at a temperature of 25 C. Assume that all parameters to solve the problem can be obtained from the given conditions except the hydrogen ion activity coefficient. Calculate the hydrogen ion activity coefficient. 12.2 A raw water containing 140 mg L of dissolved solids is subjected to coagulation treatment using alum. The hydrogen ion...

Symbols

Al(OH)2+ Al2(OH)2+ Al(OH)) Al7(OH)4+ Gram equivalents per liter of optimum alum dose First hydroxide complex of the aluminum ion Second hydroxide complex of the aluminum ion Fourth hydroxide complex of the aluminum ion Seventeenth hydroxide complex of the aluminum ion Thirty-fourth hydroxide complex of the aluminum ion Concentration of the first hydroxide complex of the aluminum ion, gmols L Concentration of the second hydroxide complex of the aluminum ion, gmols L Concentration of the fourth...

Total Effluent Nitrogen

Although the idea behind denitrification is to remove nitrogen, due to the use of sewage as a carbon source for synthesis in the heterotrophic side reaction, normal anoxic denitrification, and nitrite reduction, some ammonia is produced. These productions are indicated in Eqs. (15.31), (15.36), and (15.41). For convenience, these reactions are reproduced next 5no- + 5h+ + 5t ciohi9no3 hvno + pn2 + p- nh + 2-'jEr HCO- + pp-CO + 24f009SH2O (15.44) 3NO- + 3-H+ + C1)H19NO3 5c5hvno2 + NH + HCO- + CO...

Table 101

MCaOCaHCO3 .35 caHCO3 MTCaHCO3 M CaOMgHCO3 0.77 MgHCO3 MTMgHCO3 M CaOMgCa 2.30 MgCa MTMg M CaO MCaOCaHCO3 + M CaOMgHCO3 + M CaOMgCa + A A M CaOCO2 + M CaOExcess M sodAshCa 2.65 Ca MT Ca MsodAshMgCa 4.36 MgCa MTMg MCaCO3CaHCO3 1.23 CaHCO3MTCaHCO3 MMgOHMgHCO3 0.40 MgHCO3MTMgHCO3 MCaCO3MgHCO3 1.37 MgHCO3MTMgHCO3 M solidsCarb M Ca CaH + M MgOHMgHCO3 + M CaCO3MgHCO3 MMgOHMgCa 2.40 MgCaMTMg M solidsNonCarb MMgOHMgCa + M CaCOjCa + MCaCO3MgCa M solids M solidsCarb + M solidsNonCarb + MCaCO,CO,

Head Losses In Ion Exchangers

During ion exchange, the water or wastewater is allowed to flow through the bed. In order for this to happen, head loss allowances must be provided between influent and effluent. Ion exchanger media are actually granular, so head loss calculations are the same as those in granular filters. In addition, the mechanics of backwashing are also exactly the same as in granular filters. Rinsing may be done in downflow mode or in upflow mode. If it is done in a downflow mode, then it is the same as...

Sludge Volume Production

The mass of solids precipitated enmeshes in an enormous amount of water. As these solids are flocculated and settled, they retain extraordinary amounts of water resulting in a huge volume of sludge to be disposed of. The amount of the solids is negligible compared to the total amount of sludge. In fact, sludges contains approximately 99 water. Let fsoUds be the fraction of solids in the sludge. Then the mass of sludge Msludge is Msolids fsoUds. If Ssi is the specific gravity of the sludge, its...

Medium Specification For Granular Filters

The most important component of a granular filter is the medium. This medium must be of the appropriate size. Small grain sizes tend to have higher head losses, while large grain sizes, although producing comparatively smaller head losses, are not as effective in filtering. The actual grain sizes are determined from what experience has found to be most effective. The actual medium is never uniform, so the grain sizes are specified in terms of effective size and uniformity coefficient. Effective...

Types Of Filters

Figures 7.1 to 7.8 show examples of the various types of filters used in practice. Filters may be classified as gravity, pressure, or vacuum filters. Gravity filters are filters that rely on the pull of gravity to create a pressure differential to force the water through the filter. On the other hand, pressure and vacuum filters are filters that rely on applying some mechanical means to create the pressure differential necessary to force the water through the filter. The filtration medium may...

Characteristics of Water and Wastewater

Chapter 1 Quantity of Water and Wastewater 1.1 Probability Distribution Analysis 1.1.1 Addition and Multiplication Rules of Probability 1.1.2 Values Equaled or Exceeded 1.1.3 Derivation of Probability from Recorded Observation 1.1.4 Values Equaled or Not Exceeded 1.2 Quantity of Water 1.2.1 Design Period 1.4 Sources and Quantities of Wastewater Method 1.5.5 Graphical Comparison Method 1.6 Derivation of Design Flows of Wastewaters 1.6.1 Design Flows 1.7 Deriving Design Flows of Wastewaters from...

J[Xfi 1 [Xf[x [xf I Vmx T

ZT is the tower height and the expressions with overbars are average values between elevations 1 and 2, respectively. If the ZT's of the previous equations are solved, they will be expressed in terms of the product of the reciprocal of the overbarred factors by the respective integrals. Thus, the tower height may be expressed as the product of two factors. Consider the first as the height of a mass transfer unit, H, and the second as the number of mass transfer units, N. Therefore, H based on...

Bod

2.1.15 Nitrification in the BOD Test The general profile of oxygen consumption in a BOD test for a waste containing oxygen-consuming constituents is shown in Figure 2.1. As mentioned previously, because the nitrifiers cannot easily compete with the carbonaceous bacteria, it takes about 5 days or so for them to develop. Thus, after about 5 days the curve abruptly rises due to the nitrogenous oxygen demand, NBOD. If the nitrifiers are abundant in the beginning of the test, however, the nitrogen...

Ci

FIGURE 17.3 Chlorination for the breakdown of phenol numbers in brackets are odor threshold concentrations in Jg L. FIGURE 17.4 Proposed scheme for chloroform formation. FIGURE 17.4 Proposed scheme for chloroform formation. then is simply to chlorinate at low pH, and this in fact, would be fortunate, since HOCl predominates at low pH values instead of at high pH values. Based on this fact, if superchlorination is to be conducted, it should be done at low pH values. Further research, however,...

Water Turbine Impeller Homemade

Water Drinking Pump Impeller

FIGURE 4.1 Plan and section of a pumping station showing parallel connections. FIGURE 4.2 Pumps connected in series. unit through the eye of the impeller. This is indicated in Figure 4.2 where the Q in line meets the eye. In positive-displacement pumps, no eye exists. The left-hand side of Figure 4.3 shows an example of a positive-displacement pump. Note that the screw pump literally pushes the wastewater in order to move it. The right-hand side shows a cutaway view of a deep-well pump. This...

And Flocculation

Mixing is a unit operation that distributes the components of two or more materials among the materials producing in the end a single blend of the components. This mixing is accomplished by agitating the materials. For example, ethyl alcohol and water can be mixed by agitating these materials using some form of an impeller. Sand, gravel, and cement used in the pouring of concrete can be mixed by putting them in a concrete batch mixer, the rotation of the mixer providing the agitation....

2 y1 y2 lw

To e 22 Q 2Q (y1+y2) LW (6.31) The length L of the hydraulic jump is measured from the front face of the jump to a point on the surface of the flow immediately after the roller as shown in Figure 6.9. Experiments have shown that L 6y2 for 4 < Fr1 < 20. For Froude numbers outside this range, L is somewhat less than 6y2. For practical purposes, L may be taken as equal to 6y2. Equations (6.30) and (6.31) now become, respectively, Vjump 2 ( yi + y2 ) LW 3 y2 W ( y i + )

Alkalinity And Acidity Expressed As CaCO3

To find the equivalent concentration of alkalinity in terms of CaCO3 proceed as follows CaCO3 + 2H+ H2CO3 + Ca2+ (12.85) Note We have reacted the alkalinity species (CaCO3) with the hydrogen ion, since it is the property of alkalinity to react with an acid. From this reaction, the equivalent mass of CaCO3 is 50. Therefore, a mass equivalent of alkalinity is equal to 50 mass units expressed as CaCO3. For example, 1 gram equivalent of alkalinity is equal to 50 grams of alkalinity expressed as...

N y749

For stratified beds, Equation (7.48) must be applied layer by layer. The back-washing head losses in each layer are then summed to produce the total head loss of the bed. Thus, hLb X hLb,. le.i(1-neY)(Yp Yw) (7.50) where the index i refers to the ith layer. If x is the fraction of grain particles in layer i then lei equals xle. Thus, hLb becomes hb XhLbi le(Yp Yw)1 Xi( 1 - ne,i) (7.51) The fractional expansion of the bed may be determined by considering that the total mass of expanded and...

Backwashing Head Loss In Granular Filters

In the early development of filters, units that had been clogged were renewed by scraping the topmost layers of sand. The scraped sands were then cleaned by sand washers. In the nineteenth century, studies to clean the sand in place, rather than taking out of the unit, led to the development of the rapid-sand filter. The method of cleaning is called backwashing. In backwashing, clean water is introduced at the filter underdrains at such a velocity as to expand the bed. The expansion frees the...

Hydraulic Mixers

Hydraulic mixers are mixers that use the energy of a flowing fluid to create the power dissipation required for mixing. This fluid must have already been given the energy before reaching the point in which the mixing is occurring. What needs to be done at the point of mixing is simply to dissipate this energy in such a way that the correct value of G for effective mixing is attained. The hydraulic mixers to be discussed in this chapter are the hydraulic-jump mixer and the weir mixer. Figure 6.9...

Chemical Reaction Of The Phosphate Ion With The Ferric Salts

The chemical reaction to precipitate the phosphate ion as ferric phosphate is shown next FePO41 Fe3+ + P 4- Ksp po4 10-219 As in the case of precipitation using alum and precipitation using lime, the phosphate ion produces the set of reactions given by Eqs. (14.2) through (14.4). Let spPO Feiii be the species in solution containing the PO4 species of the orthophosphates using the ferric salts FeCl3 and Fe2(SO4)3 as the precipitants. Again, spPO FeIII will be the same as given by Equation (14.5)...

Chemical Requirements

The chemical requirements are those for the hydroxide source, chlorine, permanganate, ozone, and oxygen. The discussion will be subdivided into requirements in the ferrous reactions and into requirements in the manganous reactions. The treatment on chemical requirements, in effect, is reduced to the determination of the equivalent masses of the pertinent chemicals. 13.7.1 Requirements in the Ferrous Reactions Under these requirements are the reactions at the high and low pH ranges. At the high...

Q Ca

Solving for the head loss across the screen Ah, As shown in Equation (5.5), the value of the coefficient can be easily determined experimentally from an existing screen. In the absence of experimentally determined data, however, a value of 0.84 may be assumed for Cd. As the screen is clogging, the value of A2 will progressively decrease. As gleaned from the equation, the head loss Ah will theoretically rise to infinity. At this point, the screen is, of course, no longer functioning. The...

1

5.1 A bar screen measuring 2 m by 5 m of surficial flow area is used to protect the pump in a shoreline intake of a water treatment plant. The head loss across the screen is 0.17 m. The bar width is 20 mm and the bar spacing is 70 mm. If the screen is 30 clogged, at what rate of flow is the plant drawing water from the intake Assume Cd 0.84. 5.2 A water treatment plant drawing water at rate of 8 m s from a shoreline intake is protected by bar screen measuring 2 m by 5 m. The head loss across...

Neq

The sources of the sodium ion are the original sodium from the influent and the sodium added with the soda ash. Recall that there were MsodAsh mass of Na2CO3 used. Let this be measured in terms of kilograms. Its reaction with the Ca2+ is Na2CO3 + Ca2+ CaCO3 + 2Na+. Thus, the equivalent mass of Na2CO3 is Na2CO3 2 and the number of kilogram equivalents of the MsodAsh mass of Na2CO3 is MsodAsh (Na2CO3 2) 0.01887 MsodAsh. For the V cubic meters of water treated, the equivalent concentration in meq...

Gyi y2

Assume temperature of water 25 C then pw 997 kg m therefore, 0.048(997)(9.81)(0.94 - 0.05) J0I048) (0.94 + 0.05) - 2(9.81)(0.05)2(0.94) Example 6.4 For the problem in Example 6.3, determine if the power dissipated conforms to the requirement of effective mixing. Solution To determine if the power dissipated conforms to the criterion of effective mixing, the G value would be calculated and compared with the values of Table 6.2. Vjump 3 y2 W (y1 + y2) 3(0.94)(0.1)(0.05 + 0.94) 0.279 m3 FIGURE...

Limesoda Process

As shown by the various chemical reactions above, the chemicals soda ash and lime may be used for the removal of hardness caused by calcium and magnesium. Thus, the lime-soda process is used. This process, as mentioned, uses lime (CaO) and soda ash (Na2CO3). As the name of the process implies, two possible sets of chemical reactions are involved the reactions of lime and the reactions of soda ash. To understand more fully what really is happening in the process, it is important to discuss these...

Active Or Exchange Zone

Figure 16.2 is the same figure illustrated in a previous chapter under carbon adsorption. The length of the active zone was derived in that chapter and is reproduced next. total volume of water or wastewater treated at complete exhaustion of bed influent concentration to 8 total volume treated at time tn+1 total volume treated at time tn concentration of solute at effluent of 8 at time tn+1 concentration of solute at effluent of 8 at time tn surficial area of exchanger bed FIGURE 16.2 Active...

Colloid Destabilization

Colloid stability may further be investigated by the use Figure 12.1b. This figure portrays the competition between two forces at the surface of the colloid particle the van der Waal's force of attraction, represented by the lower dashed curve, and the force of repulsion, represented by the upper dashed curve. The solid curve represents the resultant of these two forces. As shown, this resultant becomes zero at a - a' and becomes fully an attractive force to the left of the line. When the...

Sludge Production

Sludge is composed of solids and water in such a mixture that the physical appearance looks more of being composed of wet solids than being a concentrated water. Analysis of the sludge, however, will show that it is practically water containing about 99 of it. Because of the high percentage of water that it contains, the volume of sludge produced in chemical coagulation is the biggest drawback for its use. Nevertheless, depending upon circumstances, it has to be used. Therefore, we now derive...

Q Aeration Absorption and Stripping

Aeration, absorption, and stripping are unit operations that rely on flow of masses between phases. When a difference in concentration exists between two points in a body of mass, a flow of mass occurs between the points. When the flow occurs between two phases of masses, a transfer of mass between the phases is said to occur. This transfer of mass between phases is called mass transfer. Examples of unit operations that embody the concept of mass transfer are distillation, absorption,...

Microbial Thermodynamics

The study of the relationships between heat and other forms of energy is called thermodynamics. All living things utilize heat, therefore, the science of thermodynamics may be used to evaluate life processes. An example of a life process is the growth of bacteria when wastewater is fed to them to treat the waste. Knowledge of microbial thermodynamics is therefore important to professionals involved in cleaning up wastewaters. Variables involved in the study of the relationship of heat and...

Glossary

Arithmetic method A method of predicting population that assumes the current rate of increase is constant. Average daily flow rate The mean of all daily flow values obtained from an exhaustive length of flow record. Carrying capacity One of the parameters in the factor called environmental resistance in the logistic method of predicting population. Commercial wastewater Wastewater produced in the course of conducting business. Declining-rate-of-increase method A method of predicting population...

M a50

M Ca ( hco3 )2kgeqFeii 1(00( 138.95)(1) 3.60(10-4) kgeq m3 < < 2.0(10-3) kgeq m3. Therefore, enough natural alkalinity is present and the assumption that the optimum dose is reacted in the presence of both the bicarbonate and lime is correct. Ans McaOakgeqFeII qqo13895)Pc ,3 V lReaction (12.55a) 1000(i38(9550X0.85)( 1 ) 423( 10-4) kgeq L Ans 0.004 Feno , V 0.(034(50.) ( i ) Because 6.0 mg L is greater than 1.44 mg L, enough dissolved oxygen is present in the water. 12.9.4 Chemical...

Criteria For Water Stability At Normal Conditions

In the preceding discussions, a criterion for stability was established using the equilibrium constant called Ksp. At normal conditions, as especially used in the water works industry, specialized forms of water stability criteria have been developed. These are saturation pH, Langelier index, and the precipitation potential of a given water. 11.2.1 Saturation pH and the Langelier Index Because pH is easily determined by simply dipping a probe into a sample, determination of the saturation pH is...

To Remove Or Not To Remove Nitrogen

The formula of algae is (CH2O)106(NH3)16H3PO3 (Sincero and Sincero, 1996). Gleaning from this formula, to curtail its production in any water body such as the Chesapeake Bay, it is necessary to control only any one of the elements of nitrogen, phosphorus, oxygen, hydrogen, or carbon. It must be stressed that only one needs to be controlled, because absence of any element needed for the construction of the algal body prevents the construction of the body. This is analogous to a car. To disable...

Chemical Reactions Of Alum

The alum used in water and wastewater treatment is Al2(SO4)3 14H2O. (The 14 actually varies from 13 to 18.) For brevity, this will simply be written without the water of hydration as Al2(SO4)3. When alum is dissolved in water, it dissociates according to the following equation (Sincero, 1968) Al2(SO4)3 2Al3+ + 3SO2- (12.3) By rapid mix, the ions must be rapidly dispersed throughout the tank in order to effect the complete coagulation process. FIGURE 12.5 A Phipps and Bird jar testing apparatus....

L

FIGURE 8.9 Active zones at various times during adsorption and the breakthrough curve. It is to be noted that by the nature of the process, the concentration at the bottom of the active zone as it moves through the column has to be at the limiting residual concentration. Thus, as long as has not reached the bottom of the column, the effluent is the limiting residual concentration that a particular batch of carbon is capable of removing. Figure 8.9b shows the movement of the active zone...

Ion Exchange Reactions

Ion exchange is the displacement of one ion by another. The displaced ion is originally a part of an insoluble material, and the displacing ion is originally in solution. At the completion of the process, the two ions are in reversed places the displaced ion moves into solution and the displacing ion becomes a part of the insoluble material. Two types of ion exchange materials are used the cation exchange material and the anion exchange material. The cation exchange material exchanges cations,...

Mathematics Of Mass Transfer

Between liquid and gas phases, the transfer of mass from one phase to the other must pass through the interfacial boundary surface. Call the concentration of the solute at this surface as yj referred to the gas phase. The corresponding concentration referred to the liquid phase is xj . xi and yi are the same concentration of the solute only that they are referred to different basis in effect, they are equal. Because they are equal and because the thickness of the interface is zero, xi and yi...

Oxidation Of Iron And Manganese To Reduce Precipitation pH

To summarize, the optimum pH's of precipitation are as follows ferrous removed as Fe(OH)2, 11.5 < optimum pH < 12.5 ferrous removed as Fe(OH)3, 5.5 < optimum pH < 12.5 and Mn removed as Mn(OH)2, 11.5 < optimum pH < 12.5. The reason for the high pH values for the removal of iron as Fe(OH)2 and for the removal of manganese as Mn(OH)2 is the formation of the complex ions. These ions are FeOH+ and Fe(OH)3 for the ferrous ion and Mn(OH)+, Mn(OH)0, and Mn(OH)4 for the

Table

Criteria Values for Effective Flocculation Type of Raw Water G, s-1 G to (dimensionless) Low turbidity and colored 20-70 50,000-250,000 High turbidity 70-150 80,000-190,000 FIGURE 6.11 Longitudinal section of a flocculator (top) and a blade (bottom). FIGURE 6.11 Longitudinal section of a flocculator (top) and a blade (bottom). where the size cannot go on increasing. This limiting size is the critical size and depends upon the detention time and velocity gradient. Generally, the larger velocity...

Jar Tests For Optimum pH Determination

We may summarize the optimum pH's of the coagulants obtained in the previous examples alum _ 5.32, ferrous _ 11.95, and ferric _ 8.2. The problem with these values is that they only apply at a temperature of 25 C. If the formulas for the determination of these pH's are reviewed, they will be found to be functions of equilibrium constants. By the use of the Van't Hoff equation, values at other temperatures for the equilibrium constants can be found. These, however, as mentioned before, also need...

Reaction Kinetics

The discussion so far has simply dealt with material balances. For example, they predict the concentration of nitrogen in the effluent, alkalinity requirement and production, and carbon requirement. None, however, would be able to compute the size of the reactor and how fast or how long the sewage should be treated and, although the concentrations of the nitrogen in the effluent have been predicted, the actual resulting value would depend on how long the reaction was allowed to take place. The...

Other Disinfection Formulas

The literature reveals other disinfection formulas. These include Chick's law for contact time, modifications of Chick's law, and relationship between concentration of disinfectant and concentration of microorganisms reduced in a given percentage kill. Chick's law and its modification called the Chick-Watson model, however, are not useful formulas, because they do not incorporate either the concentration of the disinfectant that is needed to kill the microorganisms or the incorporation of the...

Chemical Reactions Using Sulfur Dechlorinating Agents

Irrespective of the type of residual chlorine present, all the species can be represented by a single species by means of the equivalence of chemical reactions. It is convenient to use HOCl to represent all these species. Thus, the chemical reactions using sulfur dioxide as the dechlorinating agent with HOCl representing the residual chlorine species are as follows Sodium sulfite is Na2SO3. Thus, the chemical reactions using sodium sulfite as the dechlorination agent are as follows Na2SO3 + H2O...

Carbonate Equilibria

The carbonate equilibria is a function of the ionic strength of water, activity coefficient, and the effective concentrations of the ionic species. The equilibrium coefficients that are calculated from the species concentrations are a function of the temperature. This functionality of the coefficients can, in turn, be calculated using the Van't Hoff equation, to be addressed later. One of the major cations that can form scales as a result of the instability of water is calcium. Calcium plays an...

Pumping

Pumping is a unit operation that is used to move fluid from one point to another. This chapter discusses various topics of this important unit operation relevant to the physical treatment of water and wastewater. These topics include pumping stations and various types of pumps total developed head pump scaling laws pump characteristics best operating efficiency pump specific speed pumping station heads net positive suction head and deep-well pumps and pumping station head analysis. 4.1 pumping...

Bibliography

Pretreatment of the municipal wastewater feed for reverse osmosis plants, Desalination. 109, 2, 211-223. Abuzaid, N. S. and G. Nakhla (1997). Predictability of the homogeneous surface diffusion model for activated carbon adsorption kinetics formulation of a new mathematical model, J. Environment. Science Health, Part A Environment. Eng. Toxic Hazardous Substance Control. 32, 7, 1945-1961. Alawadhi, A. A. (1997). Pretreatment plant design Key to a successful...

[ sp po ai 3 3

Ypo4YaiI Al + Yhpo4-hpo4Yai Al + Yh2po4-h2po4-hpo4Yai Al + YP , YAl, YH, Yhp , and yh2p 4 are, respectively, the activity coefficients of the phosphate, aluminum, hydrogen, hydrogen phosphate, and dihydrogen phosphate ions. Khp , Khp , and are, respectively, the equilibrium constants of the hydro gen phosphate and dihydrogen phosphate ions and phosphoric acid. Al3+ needs to be eliminated for the equation to be expressed solely in terms of H+ . When alum is added to water, it will unavoidably...

Pressure At Pool Datum

It is instructive to derive Equation (4.44) by applying the energy equation between the wet well pool surface (point 1 of the lower tank) and the inlet to the pump (a or g). The equation is where V1 velocity at the wet pool level, z1 elevation of the pool level with reference to a datum (the pool level, itself, in this case), P1 pressure at pool level, hfs friction loss from pool level to inlet of pump (the suction side friction loss), Va velocity at inlet to the pump, za elevation of the inlet...

Water Stabilization

As mentioned in Chapter 10 on water softening, as long as the concentrations of CaCO3 and Mg(OH)2 exceed their solubilities, the solids may continue to precipitate. This condition can cause scale to form, a solid that deposits due to precipitation of ions in solution. To prevent scale formation, the water must be stabilized. A water is said to be stable when it neither dissolves nor deposits precipitates. If the pH is high, stabilization may be accomplished using one of several acids or using...

Order Of Removal

Suppose that there are four gram-equivalents of Ca2+, one gram-equivalent of Mg2+, and 2.5 gram-equivalents of HCO . Suppose further that the decision has been made to use lime. The question is which reaction takes precedence, Equation (10.15) or Equation (10.16) Assuming the former takes precedence, the bicarbonate species present will be composed of 2.5 gram-equivalent of Ca(HCO3)2 and none of the Mg(HCO3)2. The amount of lime needed to remove this bicarbonate is 2.5(CaO 2) 70 g. Assuming the...

T fica v fRm8T

Where f is the absolute viscosity of filtrate c, the mass of cake per unit volume of filtrate collected a, the specific cake resistance -AP, the pressure drop across the cake and filter So, the filter area and Rm, the filter resistance. In RO, c is the solute collected on the membrane (in the concentration boundary layer) per unit volume of permeate and Rm, the resistance of the membrane. All the other parameters have similar meanings as explained earlier in Chapter 7. The volume flux F is V...

Methods Of Disinfection And Disinfectant Agents Used

Generally, two methods of disinfection are used chemical and physical. The chemical methods, of course, use chemical agents, and the physical methods use physical agents. Historically, the most widely used chemical agent is chlorine. Other chemical agents that have been used include ozone, ClO2, the halogens bromine and iodine and bromine chloride, the metals copper and silver, KMnO4, phenol and phenolic compounds, alcohols, soaps and detergents, quaternary ammonium salts, hydrogen peroxide,...

Age of the Microorganism

The effectiveness of a disinfectant also depends upon the age of the microorganism. For example, young bacteria can easily be killed, while old bacteria are resistant. As the bacterium ages, a polysaccharide sheath is developed around the cell wall this contributes to the resistance against disinfectants. For example, when using 2.0 mg L of applied chlorine dosage, for bacterial cultures of about 10 days old, it takes 30 min of contact time to produce the same reduction as for young cultures of...

Plant Types For Hardness Removal

In practice, two types of plants are generally used for chemical precipitation hardness removal One type uses a sludge blanket contact mechanism to facilitate the precipitation reaction. The second type consists of a flash mix, a flocculation basin, and a sedimentation basin. The former is called a solids-contact clarifier. The latter arrangement of flash mix, flocculation, and sedimentation were discussed in previous chapters on unit operations. A solids-contact clarifier is shown in Figure...

Unit Processes of Water and Wastewater Treatment

10.3 Plant Types for Hardness Removal 10.4 The Equivalent CaCO3 Concentration 10.5 Softening of Calcium Hardness 10.6 Softening of Magnesium Hardness 10.7.1 Calculation of Stoichiometric Lime Required in the Lime-Soda Process 10.7.2 Key to Understanding Subscripts 10.7.3 Calculation of Stoichiometric Soda Ash Required 10.7.4 Calculation of Solids Produced 10.10 Excess Lime Treatment and Optimum Operational pH 10.11 Summary of Chemical Requirements and Solids Produced 10.13 Chemical Species in...

J1

FIGURE 3.9 Long-term extreme sewage flow and BOD pattern in a sewage treatment plant. difficulty imposed by these extreme variations, an equalization basin should be provided. Equalization is a unit operation applied to a flow for the purpose of smoothing out extreme variations in the values of the parameters. In order to produce an accurate analysis of equalization, a long-term extreme flow pattern for the wastewater flow over the duration of a day or over the duration of a suitable cycle...

R Screening Settling and Flotation

Figure Bar Screen

Screening is a unit operation that separates materials into different sizes. The unit involved is called a screen. As far as water and wastewater treatment is concerned, only two sizes of objects are involved in screening the water or wastewater and the objects to be separated out. Settling is a unit operation in which solids are drawn toward a source of attraction. In gravitational settling, solids are drawn toward gravity in centrifugal settling, solids are drawn toward the sides of cyclones...

Criteria For Effective Mixing

As the impeller pushes a parcel of fluid, this fluid is propelled forward. Because of the inherent force of attraction between molecules, this parcel drags neighboring parcels along. This is the reason why fluids away from the impeller flows even if they were not actually hit by the impeller. This force of attraction gives rise to the property of fluids called viscosity. Visualize the filament of fluid on the left of Figure 6.6 composed of several parcels strung together end to end. The motion...

Absorption And Stripping

As mentioned before, aeration is absorption. Thus, the discussions that follow apply equally to aeration (and air stripping). More specifically, the following discussions address the sizing of absorption and stripping towers. 9.6.1 Sizing of Absorption and Stripping Towers Absorption and stripping are reverse processes to each. Thus, discussing one is the same as discussing the other. Two design parameters required for the design of absorption towers are the cross section and the height. The...

Coagulation Process

The destabilization of colloids through the addition of counterions should be done in conjunction with the application of the complete coagulation process. Four methods are used to bring about this process double-layer compression, charge neutralization, entrapment in a precipitate, and intraparticle bridging. When the concentration of counterions in the dispersion medium is smaller, the thickness of the electric double layer is larger. Two approaching colloid particles cannot come close to...

Physical And Chemical Characteristics

The constituent physical and chemical characterizations to be discussed include the following turbidity (physical), color (physical), taste (physical) temperature (physical), chlorides (chemical), fluorides (chemical), iron and manganese (chemical), lead and copper (chemical), nitrate (chemical), sodium (chemical), sulfate (chemical), zinc (chemical), biochemical oxygen demand (chemical), solids (physical), pH (chemical), chemical oxygen demand (chemical), total organic carbon (chemical),...

Po4 H hpo2

HPO2- PO3-+ H+ Khpo4 10-12 3 (14.2) H2PO- HPO4- + H+ Kh2po4 10-7 2 (14.3) H3PO4 H2PO- + H+ Kh3po4 10-21 (14.4) Let sp p Al represent the species in solution containing the PO4 species of the orthophosphates, using alum as the precipitant. Therefore, spPOAl PO3- + HPO2- + H2PO- + H3PO4 (14.5) Express Equation (14.5) in terms of PO33- using Eqs. (14.2) through (14.4). This will enable spP Al to be expressed in terms of Al3+ using Equation (14.1) and Kjp,AlPO . Proceed as follows HPO4- HOT W Q 1...

Two Form Of Giardia Found In Stool

Smallest Creature Electron Microscopy

FIGURE 2.7 Life-reproductive cycle of a virus as illustrated by a T-even bacteriophage infecting a bacterial cell (a) dormancy, (b) adsorption, (c) penetration, (d) replication of new proteins and nucleic acids, (e) maturation, and (f) release and bursting of hold cell. Protozoa move through the use of the pseudopod or the use of the cilia and flagella. In pseudopodic movement, the ectoplasm flows inside the cell toward the direction of motion. As the mass of ectoplasm moves, the rear of the...

General chemistry

Chemistry is a very wide field however, only a very small portion, indeed, of this seemingly complex subject is used in this book. These include equivalents and equivalent mass, methods of expressing concentrations, activity and active concentration, equilibrium and solubility product constants, and acids and bases. This knowledge of chemistry will be used under the unit processes part of this book. The literature shows confused definitions of equivalents and equivalent masses and no universal...

Derivation of design flows of wastewaters

The accurate determination of wastewater flows is the first fundamental step in the design of wastewater facilities. To ensure proper design, accurate and reliable data must be available. This entails proper selection of design period, accurate population projection, and the determination of the various flow rates. Again, the discussion that follows addresses the particulars of the community however, parallel concerns should also be directed to the determination of industrial wastewaters and...

Pneumatic Mixers

Bubble Dissipation

Diffused aerators may also be used to provide mixing. The difference in density between the air bubbles and water causes the bubbles to rise and to quickly attain terminal rising velocities. As they rise, these bubbles push the surrounding water just as the impeller in rotational mixers push the surrounding water creating a pushing force. This force along with the rising velocity creates the power of mixing. It is evident that pneumatic mixing power is a function of the number of bubbles...

Chemical Reactions In Nitrogen Removal

In biochemical nitrogen removal, BNR, two steps are required oxidation of nitrogen to nitrate and subsequent reduction of the nitrate to gaseous nitrogen, N2. The oxidation steps are mediated by Nitrosomonas and by Nitrobacter, as mentioned previously. The reduction step is mediated by the normal heterotrophic bacteria. We will now discuss the chemical reactions involved in these oxidations and reduction. 15.6.1 Nitrification Nitrosomonas Stage From Table 15.2, the generalized donor reaction,...

Cap

Diaphragm type gage protector (typical) Diaphragm type gage protector (typical) FIGURE 17.7 Schematic of chlorine feeder system using chlorine cylinders. Following the schematic, tonne containers containing liquid chlorine are put on top of a scale in order to measure usage. Through a suitable piping, liquid chlorine under pressure flows into the evaporator. The chlorine is then evaporated into its gaseous state and conveyed into the chlorinator. The driving mechanism that abstracts the...

Unit operations and unit processes

Figure 1 shows the schematic of a conventional wastewater treatment plant using primary treatment. Raw wastewater is introduced either to the screen or to the comminutor. The grit channel removes the larger particles from the screened sewage, and the primary clarifier removes the larger particles of organic matter as well as inorganic matter that escapes removal by the grit channel. Primary treated sewage is then introduced to a secondary treatment process train downstream (not shown) where the...

Mass Transfer Units

The major purpose of dissolving air is to provide oxygen to be used by microorganism in the process of wastewater treatment. This is exemplified by the aeration employed in the activated sludge process. Aeration may also be employed for the removal of iron and manganese from groundwaters. In the removal of hardness, the presence of high concentrations of carbon dioxide may result in high cost for lime, as CO2 reacts with lime. Thus, excess concentrations of this gas may be removed from the...

Carbon Adsorption

Solids are formed because of the attraction of the component atoms within the solid toward each other. In the interior of a solid, attractive forces are balanced among the various atoms making up the lattice. At the surface, however, the atoms are subjected to unbalanced forces the ones toward the interior are attracted, but the ones at the FIGURE 8.7 Raw carbon material on the left transforms to the carbon on the right after activation. FIGURE 8.7 Raw carbon material on the left transforms to...