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Overall Rejection

The thin film composite membrane exhibited superior overall rejection performance in these tests, with ammonia and nitrate rejection showing an outstanding improvement. It has also been reported that silica rejection by the thin film composite membranes is superior to that of cellulose acetate. While the above data indicates a marginal improvement in the rejection of chemical oxygen demand (COD), which is an indication of organic content, other tests conducted by membrane manufacturers show that the polyurea and polyamide membrane barrier layers exhibit an organic rejection that is clearly superior to that of cellulose acetate. Reverse osmosis element manufacturers should be contacted for rejection data on specific organic compounds. ... [Pg.273]

Recycle experiments were designed to determine membrane fouling. Steps 1, 2, and 4 for the recycle experiments arc identical to rejection experiments, as shown in Table 7.2. In recycle experiments, step 3 involves the same amount of feed being added. No permeate samples are taken. After this cycle is completed, the permeate is returned to the stirred cell. This is repeated two times, so that the permeate has been filtered three times. At the end, one permeate sample is taken to calculate overall rejection and the concentrate is weighed and also sampled. [Pg.217]

Figure 7.49A). When a deposit of solids accumulates on the membrane surface, as is expected during ferric chloride treatment, the thickness of the unstirred boundar) layer increases (see Figure 7.49B). This means the concentration of solutes at the membrane surface increases and the overall rejection decreases. However, if the solids deposit has a positive charge (which is the case for the ferric hydroxide precipitates) then an additional barrier is added to the membrane. Solutes now have to pass through a positively charged and a negatively charged barrier, and the overall rejection will increase for some compounds. Figure 7.49A). When a deposit of solids accumulates on the membrane surface, as is expected during ferric chloride treatment, the thickness of the unstirred boundar) layer increases (see Figure 7.49B). This means the concentration of solutes at the membrane surface increases and the overall rejection decreases. However, if the solids deposit has a positive charge (which is the case for the ferric hydroxide precipitates) then an additional barrier is added to the membrane. Solutes now have to pass through a positively charged and a negatively charged barrier, and the overall rejection will increase for some compounds.
Another gas that is not rejected by RO membranes is ammonia. Ammonia is a consideration when treating wastewaters as well as feed water that has been treated with chloramine. Figure 3.2 shows the relative concentrations of ammonia gas and ammonium ion as a function of pH. At a pH of approximately 9.3, half of the ammonia species is present as ammonia gas and half as ammonium ion. The gas is not rejected, while the ion has a rejection of upwards of 80% (see Table 3.1), making the overall rejection of ammonia typically less than 50%. To achieve a relatively high rejection of ammonia, the pH of the water to the RO membranes should be less than 7-7.5, as shown in Figure 3.2. Note that ammonia gas is known to swell polyamide membranes, which causes the rejection of salts to be... [Pg.30]

The second objective is the minimization of the number of rejects (Equation 9.3). Summed over all products and time periods, it minimizes the overall rejects for all supplier-product-time period combinations. [Pg.276]

By contrast. Fig. 13.46 shows an endothermic reactor integrated below the pinch. The reactor imports Qreact from part of the process that needs to reject heat. Thus integration of the reactor serves to reduce the cold utility consumption by Qreact- There is an overall reduction in hot utility because, without integration, the process and reactor would require (Qumin + Qreact) from the utility. [Pg.331]

It was noted earlier that dryers are quite difierent in character from both distillation and evaporation. However, heat is still taken in at a high temperature to be rejected in the dryer exhaust. The appropriate placement principle as applied to distillation columns and evaporators also applies to dryers. The plus/minus principle from Chap. 12 provides a general tool that can be used to understand the integration of dryers in the overall process context. If the designer has the freedom to manipulate drying temperature and gas flow rates, then these can be changed in accordance with the plus/minus principle in order to reduce overall utility costs. [Pg.359]

TR measurements for correspondingly increased rejection of Rayleigh scattering. The addition of each grating typically introduces a throughput efficiency factor of roughly 30%, however, so that the overall efficiency of a... [Pg.2963]

The fluxes in hoUow-fiber membranes used in seawater desalination are 20—30-fold smaller, but the overall RO system size does not increase because the hoUow-fiber membranes have a much larger surface area per module unit volume. In use with seawater, their RR is about 12—17.5% and the salt rejection ratio is up to 99.5%. [Pg.250]

Assuming that the densities of the feed, the permeate and the reject are the same, one can write the following overall material balance around the module ... [Pg.266]

A gas turbine plant with an overall efficiency t]cq = 0.25 matching a heat load Acc, = 2.25 is again considered as the basic CHP plant also implied is a non-useful heat rejection ratio (Cnu)cg( cg = [1 ( cg)( g + 1)1 =. 3/16. For FESR calculations, we again take the conventional plant efficiency as 0.4 and the conventional boiler efficiency as 0.9. At the fully matched condition the.se assumptions previously led to EUF = 0.8125 and FESR = 0.2. [Pg.174]

Both approaches share two fundamental utilitarian assumptions. First, utilitarianism is a consequentialist ethics that determines right and wrong by looking to the results of various policies. Second, they hold that ethics ought to be concerned with the overall, or aggregate, welfare. Deontological ethics (the word is derived from the Greek word for duty) rejects both of these assumptions. [Pg.488]

For the condensing steam cycle, the heat rejected by the condenser is the total energy system loss and is significant with, in some cases, overall cycle efficiencies of only 25 per cent. The higher the condenser vacuum, the lower is the saturation temperature of the condensing steam in the condenser. Heat is rejected, so that the higher the vacuum, the lower is the temperature of heat... [Pg.181]

However, if the turbine back pressure is raised to above atmospheric pressure so that the turbine exhaust steam can be transported to the process heat load then the steam will give up its latent heat usefully rather than reject this to the condenser cooling water. Although the steam turbine output is reduced, the overall efficiency is increased significantly as the generated steam is used to provide both heat and electrical power. [Pg.184]

Acid addition is commonly used to convert bicarbonates into the more soluble sulfate salts to reduce the alkalinity of the RO RW, which in turn modifies the brine reject water LSI. Sometimes it is required to maintain the pH level within membrane limits. Additionally, it may be used in conjunction with a reduced dosage of antiscalent chemical to reduce the overall chemical treatment costs. [Pg.367]

In the isoenthalpic and isoentropic reaction series, the isoenthalpic and isoentropic activation parameters, respectively, may be defined as a special case of isokinetic values. Values of this kind are certainly more reliable than the usual ones in all cases when the isokinetic behavior has been proved, or, better, when it cannot be rejected. In dubious cases, when it cannot be disproved with any reliability but yet would cause a reduction of the overall accuracy, we recommend the calculation of both isokinetic and unconstrained parameters. In... [Pg.469]

The models with insignificant overall model regression as indicated by the F -value and with meaningless parameter estimates (with confidence limits) as indicated by r-values should be rejected. If rejection of the parameter does not lead to a physically nonsensical model stmcture, repeat parameter estimation and statistical analysis. [Pg.550]

On occasion, results from one of the participating laboratories will fail to meet established acceptability criteria. In those cases, acceptance or rejection of the method is determined by the CVM based on overall method performance. For example, a method that has borderline but acceptable performance for both precision and accuracy at two of three participating laboratories and fails badly at a third laboratory would probably fail. A method that was a borderline failure in one laboratory but easily passed in the other laboratories could be accepted. [Pg.93]


See other pages where Overall Rejection is mentioned: [Pg.362]    [Pg.430]    [Pg.87]    [Pg.337]    [Pg.1618]    [Pg.328]    [Pg.176]    [Pg.87]    [Pg.110]    [Pg.98]    [Pg.362]    [Pg.430]    [Pg.87]    [Pg.337]    [Pg.1618]    [Pg.328]    [Pg.176]    [Pg.87]    [Pg.110]    [Pg.98]    [Pg.194]    [Pg.1248]    [Pg.361]    [Pg.412]    [Pg.473]    [Pg.300]    [Pg.250]    [Pg.251]    [Pg.258]    [Pg.333]    [Pg.228]    [Pg.478]    [Pg.1788]    [Pg.109]    [Pg.168]    [Pg.109]    [Pg.489]    [Pg.958]    [Pg.641]    [Pg.222]    [Pg.448]    [Pg.73]   


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